CN1030620C - Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application - Google Patents

Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application Download PDF

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Publication number
CN1030620C
CN1030620C CN 92108576 CN92108576A CN1030620C CN 1030620 C CN1030620 C CN 1030620C CN 92108576 CN92108576 CN 92108576 CN 92108576 A CN92108576 A CN 92108576A CN 1030620 C CN1030620 C CN 1030620C
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China
Prior art keywords
polypropylene
fine denier
ethene
resin
tpa
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Expired - Fee Related
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CN 92108576
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Chinese (zh)
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CN1072222A (en
Inventor
陈彦模
梁伯涧
朱美芳
潘利华
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CHINESE TEXTILE UNIV
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CHINESE TEXTILE UNIV
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Priority to CN 92108576 priority Critical patent/CN1030620C/en
Publication of CN1072222A publication Critical patent/CN1072222A/en
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Publication of CN1030620C publication Critical patent/CN1030620C/en
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Abstract

The present invention relates to a resin mixture for manufacturing a polypropylene fiber modified fine denier filament and a super fine denier filament and a blending method thereof. The resin mixture is formed by directly blending polypropylene with controllable rheological properties, copolymerized polyester, etc. The fine denier filament of which the monofilament fineness is from 0.3 to 1.3 dtex, and the super fine denier filament can be prepared by the resin mixture. The fiber which is spun can be dyed by dispersion dye sold in the market at normal pressure, and the moisture absorption rate of a fabric is higher than that of terylene, which conforms to the processing requirement of fabrics comprising sportswear, underclothes, spring and autumn face fabric, etc.

Description

Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application
The present invention relates to be used to make the resin compound and the blend method thereof of polypropylene fibre modification fine denier filament and superfine denier fiber.
The fiber of producing by plain polypropylene as take fibrous material because of stainability, hygroscopicity is relatively poor and the sense of fabric wax shape fails to obtain extensive use for a long time.In recent years, because with the thin dawn of special processing method production and the development of super fine denier (filament number is less than 1 dtex) polypropylene fibre, thereby give the significant saturating wet perspiration discharging performance of polypropylene fabric and be widely used in underclothes, as high-grade gym outfit, underwear and spring and autumn clothing lining.Yet the method that present polypropylene fibre all adopts the interpolation Masterbatch to prepare coloured remedies the defective that polypropylene fibre is difficult to dye, and commercially available acrylic resin can only spin the fiber of filament number greater than 1.3 dtexs with general spining technology.
According to JP02,191,719 reports, the composite fibre of the copolymer (CDPET) of general fibrous polypropylene and sodiosulfoisophthalic acid-terephthalic acid (TPA), after alkali treatment, dissolve the CDPET component, can make the superfine fibre that filament number is 0.22d, as filtration fabrics, this invention does not relate to the application that blending type is taken fiber.
The present invention will control blending and modifyings such as the controllable rheology acrylic resin of polymer streams sex change and CDPET with molecular-weight adjusting, make its prepared fiber have the disperse dyes stainability.Because the polypropylene modified fiber filament number that the present invention makes is 0.3~1.3 dtex, thereby make fabric have the good wicking effect, present significant saturating wet perspire, more opened up the Application Areas of polypropylene fibre, can be used as top grade and take fibrous material, even surpass some natural fabric.
Technical essential of the present invention is: a kind of polypropylene modification resin, form by polypropylene and one or more other resins, described polypropylene is the resin with controllable rheology, its melt index 〉=20 restrain/10 fens, inherent viscosity [η] is 1.25~1.55, and described other resins are that inherent viscosity [η] is that 0.5~0.61 sodiosulfoisophthalic acid and copolyester, ethylene-vinyl acetate copolymer and the ethylene-acrylic acid copolymerization zinc salt of terephthalic acid (TPA), the percentage by weight of its prescription are:
Polypropylene 80~95
Copolyester 5~20
Ethene-acetate ethylene copolymer 0~7
Ethene-acrylic copolymer zinc salt 0~4
The optimum formula of polypropylene modification resin is made up of the controllable rheology polypropylene of weight ratio 90% and 10% sodiosulfoisophthalic acid and terephthalic acid (TPA) copolyester.
The optimum formula of polypropylene modification resin is made up of the controllable rheology polypropylene of weight ratio 85%, 10% sodiosulfoisophthalic acid and the ethylene-vinyl acetate copolymer of terephthalic acid (TPA) copolyester and 5%.
The optimum formula of polypropylene modification resin is made up of the controllable rheology polypropylene of weight ratio 80%, 19% sodiosulfoisophthalic acid and the ethylene-acrylic acid copolymer zinc salt of terephthalic acid (TPA) copolyester and 1%.
The production method of polypropylene modification resin of the present invention is to be delivered in the double screw extruder fusion under 270 ℃ of temperature, Cast Strip and pelletizing by weight with after the direct blend of above-mentioned resin.
With above-mentioned polypropylene modification resin slicer melt spinning, spin under the speed at 400~1100 meters/minute, stretch 3~5 times between room temperature to 120 ℃, can be made into fine denier filament and superfine denier fiber that stainability and filament number are 0.3~1.3 dtex.
Compare prior art, the present invention has following advantage:
The present invention altogether the fiber that spinned of warm modified polypropylene resin can carry out dyeing at normal pressure with commercially available DISPERSE DYES, have good color tone.Measured by colour photometer, with Disperse Red 3B dyeing, the KS value brings up to 3.61 by 0.63 of virgin pp, and to disperse blue 2BLN dyeing, the KS value brings up to 6.40 by 0.62.
2. the fiber that when containing the CDPET of 10% weight ratio in the modified resin, spins, after alkali treatment, polyacrylic hygroscopicity can bring up to 0.521% by original 0.02%, than hygroscopicity 0.4% height of terylene, and has overcome the wax shape sense of polypropylene fibre fabric to a certain extent.
3. to spin the fibre single thread fiber number that the super drawing method produces be 0.3~1.3 dtex by common in the present invention, intensity 〉=4 newton/dtex, degree of stretching≤60%.Meet sweat shirt, underwear and spring and autumn fabric processing request such as lining.
Below the present invention is further elaborated by three examples:
Example one:
The CDPET section was dried 48 hours in 100 ℃ under the vacuum of 760mmHg post, with 90: 10 weight ratios with above-mentioned controllable rheology polypropylene and CDPET mixed after, under 270 ℃, melt blending and the granulation of system band in Branbender ZSK 30M9/II double screw extruder.Blending extrudant is observed under ESEM, for having equally distributed fento-matrix structure (seeing photo), the maximum particle diameter of CDPET decentralized photo<3 micron, melt-spun under 400 meters/minute, making intensity 〉=4 newton/dtex, degree of stretching≤80%, fiber number is the fiber of 0.7 dtex.
Example two:
CDPET ethylene-vinyl acetate copolymer after above-mentioned controllable rheology polypropylene and the vacuumize is mixed with 85: 10: 5 weight ratios, is with granulation at Branbender ZSK 30M9/II double screw extruder melt blending and system under 270 ℃.The blending extrudant that obtains is observed under ESEM, has uniform distribution (photo 2), the maximum particle diameter of decentralized photo<2.3 micron, and the fiber number that makes fiber is 1 dtex.
Example three:
CDPET ethylene-acrylic acid copolymer zinc salt after above-mentioned controllable rheology polypropylene and the vacuumize was with weight ratio blend granulation in 80: 19: 1, the blending extrudant that is obtained is observed under ESEM, its blend be improved (photo 3) that distribute, decentralized photo maximum particle diameter<2 micron, the fiber number that makes fiber is 1.3 dtexs.

Claims (5)

1, a kind of polypropylene fine denier and super fine denier blending resin, form by polypropylene and one or more other resins, it is characterized in that described polypropylene is the resin with controllable rheology, its melt index>20 restrain/10 fens, inherent viscosity [η] is 1.25~1.55, and described other resin properties viscosity [η] are that 0.5~0.61 sodiosulfoisophthalic acid and copolyester, ethene-acetate ethylene copolymer and the ethene-acrylic copolymer zinc salt of terephthalic acid (TPA), the percentage by weight of its prescription are:
Polypropylene 80~95
Copolyester 5~20
Ethene-acetate ethylene copolymer 0~7
Ethene-acrylic copolymer zinc salt 0~4
2,, it is characterized in that described optimum formula is made up of benzene two methanesulfonic sodiums and terephthalic acid (TPA) copolymerization polyester between the controllable rheology polypropylene of weight ratio 90% and 10% according to described polypropylene fine denier of claim 1 and super fine denier blending resin.
3, according to described polypropylene fine denier of claim 1 and super fine denier blending resin, it is characterized in that described optimum formula is the controllable rheology polypropylene by weight ratio 85%, 10% the M-phthalic acid sulphur sodium and the ethene-acetate ethylene copolymer of terephthalic acid (TPA) copolymerization polyester and 5% are formed.
4, according to described polypropylene fine denier of claim 1 and super fine denier blending resin, it is characterized in that described optimum formula is the controllable rheology polypropylene by weight ratio 80%, 19% M-phthalic acid sulphur sodium and the ethene of terephthalic acid (TPA) copolymerization polyester and 1%-acrylic copolymer zinc salt are formed.
5, set the stainability of vinegar preparation and the fine denier filament and the superfine denier fiber of filament number 0.3~1.3 dtex with each described polypropylene fine denier of claim 1-4 and super fine denier with blend.
CN 92108576 1992-09-29 1992-09-29 Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application Expired - Fee Related CN1030620C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 92108576 CN1030620C (en) 1992-09-29 1992-09-29 Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 92108576 CN1030620C (en) 1992-09-29 1992-09-29 Blended resin for the use of polypropylene fibre fine denier yarn and superfine denier yarn, production and application

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CN1072222A CN1072222A (en) 1993-05-19
CN1030620C true CN1030620C (en) 1996-01-03

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100406623C (en) * 2006-07-18 2008-07-30 东华大学 Process for preparing polypropylene/polyester alloy fiber

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1064416C (en) * 1996-05-02 2001-04-11 上海石油化工股份有限公司 Method for manufacturing dyeable fine denier polypropylene fibre
CN1068640C (en) * 1997-09-24 2001-07-18 山东虎山实业集团有限公司 Process for producing fine denier polypropylene fiber short-staple
TW579394B (en) * 2001-04-24 2004-03-11 Rhodia Industrial Yarns Ag Process for the production of fine monofilaments made from polypropylene, fine monofilaments made from polypropylene, and their application

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100406623C (en) * 2006-07-18 2008-07-30 东华大学 Process for preparing polypropylene/polyester alloy fiber

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