WO2006070970A1 - Dope dyed flame retardant polyester fibers, textle products therefrom and the method of manufacturing thereof - Google Patents

Dope dyed flame retardant polyester fibers, textle products therefrom and the method of manufacturing thereof Download PDF

Info

Publication number
WO2006070970A1
WO2006070970A1 PCT/KR2005/000987 KR2005000987W WO2006070970A1 WO 2006070970 A1 WO2006070970 A1 WO 2006070970A1 KR 2005000987 W KR2005000987 W KR 2005000987W WO 2006070970 A1 WO2006070970 A1 WO 2006070970A1
Authority
WO
WIPO (PCT)
Prior art keywords
flame retardant
dope
retardant polyester
polyester
dyed
Prior art date
Application number
PCT/KR2005/000987
Other languages
French (fr)
Inventor
Seung Cheol Yang
Eung Soo Kim
Yang Kuk Son
Original Assignee
Hyosung Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hyosung Corporation filed Critical Hyosung Corporation
Priority to US11/792,681 priority Critical patent/US20080268736A1/en
Priority to EP05733515A priority patent/EP1831443A4/en
Priority to JP2007549229A priority patent/JP2008525661A/en
Publication of WO2006070970A1 publication Critical patent/WO2006070970A1/en

Links

Classifications

    • 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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/07Addition of substances to the spinning solution or to the melt for making fire- or flame-proof filaments
    • 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
    • D01F1/00General methods for the manufacture of artificial filaments or the like
    • D01F1/02Addition of substances to the spinning solution or to the melt
    • D01F1/04Pigments
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01DMECHANICAL METHODS OR APPARATUS IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS
    • D01D5/00Formation of filaments, threads, or the like
    • D01D5/28Formation of filaments, threads, or the like while mixing different spinning solutions or melts during the spinning operation; Spinnerette packs therefor
    • D01D5/30Conjugate filaments; Spinnerette packs therefor
    • DTEXTILES; PAPER
    • D01NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01FCHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • DTEXTILES; PAPER
    • 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
    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06BTREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B3/00Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
    • D06B3/04Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of yarns, threads or filaments
    • 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]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S57/00Textiles: spinning, twisting, and twining
    • Y10S57/904Flame retardant
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T442/00Fabric [woven, knitted, or nonwoven textile or cloth, etc.]
    • Y10T442/30Woven fabric [i.e., woven strand or strip material]
    • Y10T442/3976Including strand which is stated to have specific attributes [e.g., heat or fire resistance, chemical or solvent resistance, high absorption for aqueous composition, water solubility, heat shrinkability, etc.]
    • Y10T442/3984Strand is other than glass and is heat or fire resistant

Definitions

  • the present invention relates to a dope-dyed flame retardant polyester fiber, textile products made therefrom, and the method of manufacturing the same.
  • Conventional methods of imparting flame retardancy to dope-dyed fibers may be broadly divided into a method involving flame retardancy by post-treament and a method involving making fiber materials flame retardant, thereby imparting permanently flame retardant materials.
  • the conventional method using flame retardancy post-treament to impart flame retardancy has been conventionally performed on natural fibers such as cotton and is also employed in the production of flame retardant synthetic fibers.
  • the method of imparting flame retardancy via post-treatment presents problems associated with durability, and occurrence of environmental problems due to waste water generated during treatment. As such, this method is now widely used but would be phased out due to the increase of environmental interest.
  • bromine based flame retardants may give off carcinogenic substances such as dioxin and benzofuran, there is a movement towards regulation of brominated flame retardants, thereby actively facilitating substitution with the phosphorus based flame retardants.
  • polyester fibers prepared using the above-mentioned patent methods lack UV stability and thus suffer from deterioration of flame retardancy durability and physical properties of the fibers upon prolonged exposure to sunlight. Meanwhile, intrinsic properties of polyester fibers make it difficult to impart them with deep colors by dyeing. In addition, polyester fibers exhibit low fastness because fibers and dyes are not bound by chemical bonding. That is, as can be seen from their polymer structures, polyester fibers do not have reactive groups capable of undergoing chemical reaction, such as hydroxyl groups or amide groups.
  • polyester fibers have a disadvantage that they are dyed only by disperse dyes. Since adsorbed dyes are not chemically bound to the fibers, the dyes may be separated from the fibers upon exposure to high temperatures or organic solvents such as N,N-dimethyl formamide.
  • a large number of methods have been proposed to blend pigments or dyes into fibers during fiber formation.
  • production of fibers having various colors is not suitable for industrial and large-scale production and thereby, among various colors, only dark black colored yarns have been produced in industrial and large-scale.
  • dope-dyed filaments have been produced to exhibit deep black color and to solve fastness problems. Reference may be made to the following methods of producing dope-dyed filaments .
  • a method involving introducing dyes or pigments during a polymerization process serves to make special polymers by introducing dyes or pigments during polymerization.
  • Dyes or pigments are generally provided as fine powders .
  • ethylene glycol hereinafter, referred to as "EG"
  • EG ethylene glycol
  • liquid dyes or pigments are introduced alone or diluted in EG prior to introduction.
  • This method is advantageous for preparing uniformly dispersed polymer products, but suffers from contamination of polymerization apparatuses with dyes or pigments. In particular, when a batch process is employed to prepare polymer products, color difference between batches may occur and contamination of polymerization apparatuses makes it difficult to produce different kinds of polymer products in the same apparatus .
  • This method involves blending a master batch, containing a high concentration of pigments or dyes, with conventional polyester polymers, followed by spinning, and is simple.
  • black color products can be prepared by blending a master batch containing a large amount of carbon black with conventional polyester polymers.
  • spinning workability and properties of the resulting fibers vary depending upon kinds of base resins in the master batch (polymers used in the mater batch) , selection of the master batch and optimal content is important.
  • the present invention has been made in view of the above problems, and it is an object of the present invention to provide a dope-dyed flame retardant polyester fiber having permanent flame retardancy, superior flame retardancy durability and UV stability, and high fastness by introduction of pigments into fiber itself, a method of preparing thereof, and fiber products having excellent flame retardancy and light shieldability, such as blackout curtains, using the same .
  • a dope-dyed flame retardant polyester fiber comprising 500 to 5000 ppm of carbon black in a flame retardant polyester polymer containing 500 to 50000 ppm of a phosphorus based flame retardant based on phosphorus atoms .
  • the present inventors have conducted tests on a variety of flame retardants in order to impart permanent flame retardancy to polyester fibers.
  • flame retardants which are industrially used to impart flame retardancy, are broadly classified into halogen based flame retardants and phosphorus based flame retardants.
  • the halogen based flame retardants are known to exhibit superior flame retardancy to the phosphorus based flame retardants, but the halogen based flame retardants, represented primarily by bromine, give off carcinogenic substances such as dioxin upon burning and thus regulations on use thereof are gradually being instituted.
  • the phosphorus based flame retardants are broadly divided into main-chain type flame retardants in which flame retardancy-imparting phosphorus atoms are directly attached to polyester backbones and side-chain type flame retardants in which phosphorus atoms are attached to polyester backbones via side chains.
  • the present inventors have discovered a flame retardant represented by the following general formula 1, as a side-chain type flame retardant that exhibits excellent resistance to hydrolysis.
  • the side-chain type flame retardant represented by the following general formula 1 has reactive groups capable of undergoing esterification or transesterification in its own molecular structure and thus is co-polymerizable with polyethylene terephthalate.
  • base polyester polymer resins that can be used in the present invention, mention may be made of polyethylene terephthalate, polybutylene terephthalate, copolymerized polyethylene terephthalate containing 12 mol% or less of isophthalic acid, or a copolymerized polybutylene terephthalate resin containing 12 mol% or less of isophthalic acid.
  • the content of the flame retardant of general formula 1 in the polymer is in the range of 500 to 50,000 ppm, and more preferably 1,000 to 20,000 ppm, based on phosphorus atoms. Where the phosphorus atom content is less than 500 ppm, desired flame retarding effects cannot be obtained. In contrast, the phosphorus atom content greater than 50,000 ppm undesirably results in difficulty to increase the degree of polymerization of the resulting polyester and remarkably reduces crystallinity, thereby making it difficult to produce fibers or films.
  • R 1 and R 2 are independently hydrogen or a different or same radical having a ⁇ -hydroxyl group and containing 2 to 4 carbon atoms, and p is an integer between 1 and 5.
  • the present invention is intended for light shielding, and thus stability of the polymer upon exposure to sunlight, in particular UV light, is of primary importance. As such, UV stability is certainly necessary and thereby it is important to add a UV stabilizer.
  • manganese phosphate is most effective.
  • manganese phosphate is insoluble in ethylene glycol, thereby making it difficult to be incorporated into the polymer. Therefore, the present inventors have found that it is most proper to synthesize manganese phosphate in a reaction system by separately introducing manganese acetate and phosphoric acid to the reactor, instead of directly introducing manganese phosphate into a reactor.
  • the content of manganese acetate utilized for synthesis of manganese phosphate is preferably in the range of 0.1 to 500 ppm, and more preferably 0.2 to 200 ppm, based on manganese atoms in the polymer. If the content of manganese acetate is below 0.1 ppm, it is difficult to obtain the desired UV stability. If the content of manganese acetate exceeds 500 ppm, problems associated with dispersibility arise, thereby leading to increased pack pressure upon spinning.
  • the content of phosphoric acid is preferably in the range of 0.1 to 500 ppm, and more preferably 0.2 to 200 ppm based on the phosphorus atom content relative to the polymer.
  • phosphorus based materials may be added in any amount, so long as the reaction between the phosphorus material and the manganese salt is not inhibited, concentrations greater than 500 ppm may lead to decreased catalytic activity, thereby it making difficult to prepare the desired flame retardant polyester.
  • the present invention has selected a method using a master batch.
  • selection of a base resin constituting the master batch is important.
  • the base resin of the master batch even when it was blended in a small amount with flame retardant polyester polymers, caused color differences if the base resin was incompatible with the flame retardant polymer.
  • the difference in heat resistance between the base resin and polyester polymers is large, it was found that qualities of the resulting products were deteriorated in a manufacturing process and post-processing of fibers.
  • the base resin of the master batch should be compatible with the flame retardant polyester polymer utilized in the present invention and satisfy the following inequality 1 in order to obtain excellent processability in a spinning process and the like:
  • T FR is a melting point of the flame retardant polyester polymer and T B is a melting point of the base resin of the master batch.
  • T m is a melting point of the prepared fiber, excluding the case in which the number of melting point peaks is two or more.
  • T m melting point of the prepared fiber
  • T m heat resistance is lowered and thus fusion of fibers and tight spots tend to occur in post-processing.
  • T m is higher than 250 ° C
  • another melting peak is developed due to phase separation, thereby it is difficult to obtain fibers having uniform physical properties and it is difficult to prepare products having uniform colors.
  • suitable content of carbon black is between 500 and 5000 ppm, relative to the flame retardant polyester fibers. If the content of carbon black is less than 500 ppm, it is difficult to develop desired colors and it is also difficult to effect uniform blending, thereby resulting in occurrence of inferior dyeing. Whereas, if the content of carbon black is higher than 5000 ppm, the amount of carbon black added is too much, thus leading to increased production costs and deterioration of spinnability.
  • the spinning process in accordance with the present invention is a spin-draw process whereby drawing is performed in conjunction with spinning, it is also possible to perform drawing or false twisting after preparing partially oriented yarns (POY) .
  • a slurry of 8650 g of terephthalic acid (hereinafter, referred to as "TPA”) and 2700 g of ethylene glycol (hereinafter, referred to as "EG”) was subjected to esterification using a semi-batch process.
  • Oligomers prepared to have the same composition as in the slurry were stirred in an esterification reactor while the temperature of the reactor was maintained at 250 to 260 ° C. After completion of slurry introduction, esterification was additionally progressed for 30 minutes, thereby reaching an esterification reaction rate of 96.5%.
  • the prepared oligomers were transferred to a polycondensation reactor.
  • a EG solution in which the concentration of a compound of a general formula 1 (wherein p is 1, Ri and R 2 are CH 2 CH 2 OH) was 65 weight % was used. 1380 g of the flame retardant solution was introduced to the reactor, and then manganese acetate and phosphoric acid, as UV stabilizers, were added to the reactor with the concentrations of 44 ppm and 75 ppm, respectively, based on manganese and phosphorus atoms. Next, as a catalyst,
  • a master batch was prepared to contain 30% by weight of carbon black using respective polymers listed in Table 1 and a twin extruder.
  • the prepared flame retardant polyester polymers and the master batches having the same composition as shown in Table 1 were subjected to spinning and yarn processing so as to prepare dope-dyed flame retardant polyester fibers.
  • Comparative Example 4 This example was carried out using the same procedure as in Example 1, except that flame retardant polyester polymers were prepared to have phosphorus content of 280 ppm.
  • Master batch content wt% of master batch upon blending (weight of master batch/ (weight of master batch + weight of flame retardant polyester polymer) x 100)
  • dope-dyed flame retardant polyester fibers in accordance with the present invention have excellent flame retardancy, UV stability and fastness.
  • use of fibers in accordance with the present invention in preparing blackout curtains or the like can simultaneously provide excellent flame retardancy and light shieldability.

Landscapes

  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Artificial Filaments (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Woven Fabrics (AREA)

Abstract

The present invention relates to dope dyed flame retardant polyester fibers, textile products therefrom, and the method of manufacturing thereof. The polyester fiber comprises flame retardant polyester polymers containing 500 - 50,000ppm of phosphorus-based flame retardant agent based on phosphorus atom, and 500 5,000ppm of carbon black based on said polyester polymers. The polyester fibers can provide excellent fastness and flame retardant characteristic without occurring hazardous, materials such as a dioxin during an incineration, and can be applied for fiber products such as blackout curtain having an effective light shielding.

Description

[DESCRIPTION] [Invention Title]
DOPE DYED FLAME RETARDANT POLYESTER FIBERS, TEXTILE PRODUCTS THEREFROM AND THE METHOD OF MANUFACTURING THEREOF
[Technical Field]
The present invention relates to a dope-dyed flame retardant polyester fiber, textile products made therefrom, and the method of manufacturing the same.
[Background Art]
Conventional methods of imparting flame retardancy to dope-dyed fibers may be broadly divided into a method involving flame retardancy by post-treament and a method involving making fiber materials flame retardant, thereby imparting permanently flame retardant materials.
The conventional method using flame retardancy post-treament to impart flame retardancy has been conventionally performed on natural fibers such as cotton and is also employed in the production of flame retardant synthetic fibers. However, the method of imparting flame retardancy via post-treatment presents problems associated with durability, and occurrence of environmental problems due to waste water generated during treatment. As such, this method is now widely used but would be phased out due to the increase of environmental interest.
In addition, as to the method involving rendering fiber materials permanently flame retardant, a method of imparting flame retardancy by copolymerization is primarily employed. For this purpose, reactive copolymerizable flame retardants are also variously commercialized.
Methods of forming flame retardant polyesters via copolymerization largely rely upon bromine (Br) -based flame retardants and phosphorus (P) -based flame retardants. As to patented inventions using bromine- based flame retardants, reference is made to Japanese Patent Publication Laid-open Nos. Sho 62-6912, 53-46398 and 51-28894. In this connection, bromine based compounds are susceptible to thermal degradation at high temperatures, and thus, a large quantity of flame retardants must be added in order to achieve effective flame retardancy. As a result, color and light fastness of the resulting polymeric material are deteriorated. In addition, due to the recent presentation of the possibility that bromine based flame retardants may give off carcinogenic substances such as dioxin and benzofuran, there is a movement towards regulation of brominated flame retardants, thereby actively facilitating substitution with the phosphorus based flame retardants.
As to patented inventions using phosphorus-based flame retardants, reference is made to US Patent Nos . 3941752, 5899428 and 5180793, and Japanese Patent Publication Laid-open No. Sho 50-56488. Reactive flame retardants disclosed in these patents have disadvantages such as deterioration of physical properties due to hydrolysis upon post-treatment, in particular dyeing polyester fibers, because phosphorus atoms are bound to a main chain or backbone of the polymer. Because the P-O linkage has a somewhat lower bond energy than any other linkage in copolyester polymer. In addition, flame retardant polyester fibers prepared using the above-mentioned patent methods lack UV stability and thus suffer from deterioration of flame retardancy durability and physical properties of the fibers upon prolonged exposure to sunlight. Meanwhile, intrinsic properties of polyester fibers make it difficult to impart them with deep colors by dyeing. In addition, polyester fibers exhibit low fastness because fibers and dyes are not bound by chemical bonding. That is, as can be seen from their polymer structures, polyester fibers do not have reactive groups capable of undergoing chemical reaction, such as hydroxyl groups or amide groups.
Therefore, polyester fibers have a disadvantage that they are dyed only by disperse dyes. Since adsorbed dyes are not chemically bound to the fibers, the dyes may be separated from the fibers upon exposure to high temperatures or organic solvents such as N,N-dimethyl formamide. In order to solve such problems, a large number of methods have been proposed to blend pigments or dyes into fibers during fiber formation. However, production of fibers having various colors is not suitable for industrial and large-scale production and thereby, among various colors, only dark black colored yarns have been produced in industrial and large-scale. Further, since it is difficult to effect deep black color dyeing with general dyeing methods, dope-dyed filaments have been produced to exhibit deep black color and to solve fastness problems. Reference may be made to the following methods of producing dope-dyed filaments .
Firstly, there is a method involving introducing dyes or pigments during a polymerization process. This method serves to make special polymers by introducing dyes or pigments during polymerization. Dyes or pigments are generally provided as fine powders . Accordingly, ethylene glycol (hereinafter, referred to as "EG") is used to dissolve or disperse the dyes or pigments for introduction. In addition, liquid dyes or pigments are introduced alone or diluted in EG prior to introduction. This method is advantageous for preparing uniformly dispersed polymer products, but suffers from contamination of polymerization apparatuses with dyes or pigments. In particular, when a batch process is employed to prepare polymer products, color difference between batches may occur and contamination of polymerization apparatuses makes it difficult to produce different kinds of polymer products in the same apparatus .
Secondly, there is a method involving blending and spinning master batches. This method involves blending a master batch, containing a high concentration of pigments or dyes, with conventional polyester polymers, followed by spinning, and is simple. In particular, black color products can be prepared by blending a master batch containing a large amount of carbon black with conventional polyester polymers. In this method, since spinning workability and properties of the resulting fibers vary depending upon kinds of base resins in the master batch (polymers used in the mater batch) , selection of the master batch and optimal content is important.
Thirdly, there is a method involving fiber dyeing and post-processing. This method is performed by adsorbing an excess amount of black pigments or dyes on a surface of the prepared polyester fibers at a high temperature, followed by drying, or fixing them on the fiber surface by crosslinking, in order to enhance fastness. This method is not widely employed due to its very high production costs, low productivity, and difficulty in the uniformity of the products. Meanwhile, Japanese Patent Publication Laid-open Nos. Hei 3-137227, 3-137228, 10-77523 and 3-131051 propose methods of producing dope-dyed fibers using pigments such as carbon black in fibers . These methods primarily relate to production of nylon for fishing nets or high tenacity yarns such as seat belts, and thus are not suited for dope-dyed flame retardant polyester fibers as are the aim of the present invention. As described above, there have been known methods of imparting flame retardancy to polyester fibers or methods of increasing fastness by preparing dope-dyed filaments, respectively, but a method of simultaneously imparting two functionalities, while having UV stability and light shieldability, is not yet known in the art.
[Disclosure] [Technical Problem]
Therefore, the present invention has been made in view of the above problems, and it is an object of the present invention to provide a dope-dyed flame retardant polyester fiber having permanent flame retardancy, superior flame retardancy durability and UV stability, and high fastness by introduction of pigments into fiber itself, a method of preparing thereof, and fiber products having excellent flame retardancy and light shieldability, such as blackout curtains, using the same .
[Technical Solution]
In accordance with the present invention, the above and other objects can be accomplished by the provision of a dope-dyed flame retardant polyester fiber, comprising 500 to 5000 ppm of carbon black in a flame retardant polyester polymer containing 500 to 50000 ppm of a phosphorus based flame retardant based on phosphorus atoms .
Other objects, particular advantages and novel characteristics of the present invention will be more clear from the following detailed description and preferred embodiments.
[Best Mode]
Construction of dope-dyed flame retardant polyester fibers in accordance with the present invention will now be described.
The present inventors have conducted tests on a variety of flame retardants in order to impart permanent flame retardancy to polyester fibers. Currently, flame retardants, which are industrially used to impart flame retardancy, are broadly classified into halogen based flame retardants and phosphorus based flame retardants. The halogen based flame retardants are known to exhibit superior flame retardancy to the phosphorus based flame retardants, but the halogen based flame retardants, represented primarily by bromine, give off carcinogenic substances such as dioxin upon burning and thus regulations on use thereof are gradually being instituted.
In addition, the phosphorus based flame retardants are broadly divided into main-chain type flame retardants in which flame retardancy-imparting phosphorus atoms are directly attached to polyester backbones and side-chain type flame retardants in which phosphorus atoms are attached to polyester backbones via side chains.
The present inventors have discovered a flame retardant represented by the following general formula 1, as a side-chain type flame retardant that exhibits excellent resistance to hydrolysis.
The side-chain type flame retardant represented by the following general formula 1 has reactive groups capable of undergoing esterification or transesterification in its own molecular structure and thus is co-polymerizable with polyethylene terephthalate.
As base polyester polymer resins that can be used in the present invention, mention may be made of polyethylene terephthalate, polybutylene terephthalate, copolymerized polyethylene terephthalate containing 12 mol% or less of isophthalic acid, or a copolymerized polybutylene terephthalate resin containing 12 mol% or less of isophthalic acid.
The content of the flame retardant of general formula 1 in the polymer is in the range of 500 to 50,000 ppm, and more preferably 1,000 to 20,000 ppm, based on phosphorus atoms. Where the phosphorus atom content is less than 500 ppm, desired flame retarding effects cannot be obtained. In contrast, the phosphorus atom content greater than 50,000 ppm undesirably results in difficulty to increase the degree of polymerization of the resulting polyester and remarkably reduces crystallinity, thereby making it difficult to produce fibers or films.
Figure imgf000012_0001
Formula 1 wherein R1 and R2 are independently hydrogen or a different or same radical having a ω -hydroxyl group and containing 2 to 4 carbon atoms, and p is an integer between 1 and 5.
Further, the present invention is intended for light shielding, and thus stability of the polymer upon exposure to sunlight, in particular UV light, is of primary importance. As such, UV stability is certainly necessary and thereby it is important to add a UV stabilizer.
As a result of various tests, the present inventors have found that manganese phosphate is most effective. However, manganese phosphate is insoluble in ethylene glycol, thereby making it difficult to be incorporated into the polymer. Therefore, the present inventors have found that it is most proper to synthesize manganese phosphate in a reaction system by separately introducing manganese acetate and phosphoric acid to the reactor, instead of directly introducing manganese phosphate into a reactor.
The content of manganese acetate utilized for synthesis of manganese phosphate is preferably in the range of 0.1 to 500 ppm, and more preferably 0.2 to 200 ppm, based on manganese atoms in the polymer. If the content of manganese acetate is below 0.1 ppm, it is difficult to obtain the desired UV stability. If the content of manganese acetate exceeds 500 ppm, problems associated with dispersibility arise, thereby leading to increased pack pressure upon spinning.
In addition, the content of phosphoric acid is preferably in the range of 0.1 to 500 ppm, and more preferably 0.2 to 200 ppm based on the phosphorus atom content relative to the polymer. Although phosphorus based materials may be added in any amount, so long as the reaction between the phosphorus material and the manganese salt is not inhibited, concentrations greater than 500 ppm may lead to decreased catalytic activity, thereby it making difficult to prepare the desired flame retardant polyester.
In the present invention, tests were focused on enhancement of fastness of black color in the flame retardant polyester fibers. Direct introduction of pigments or dyes into a polymerization process undesirably presented problems such as contamination of polymerization apparatuses and color difference between batches. In addition, in a fiber dyeing method, it was difficult to select pigments or dyes showing affinity for polyester fibers. When resins were added to fibers, followed by curing, in order to increase fixing capacity of pigments or dyes, the resulting fibers exhibited high rigidity, and reduced flame retardancy.
As such, the present invention has selected a method using a master batch. In the present invention, it was found that selection of a base resin constituting the master batch is important. The base resin of the master batch, even when it was blended in a small amount with flame retardant polyester polymers, caused color differences if the base resin was incompatible with the flame retardant polymer. In addition, where the difference in heat resistance between the base resin and polyester polymers is large, it was found that qualities of the resulting products were deteriorated in a manufacturing process and post-processing of fibers. The base resin of the master batch should be compatible with the flame retardant polyester polymer utilized in the present invention and satisfy the following inequality 1 in order to obtain excellent processability in a spinning process and the like:
TFR - 20°C < TB ≤ TFR + 20°C 1 wherein TFR is a melting point of the flame retardant polyester polymer and TB is a melting point of the base resin of the master batch.
220°C < Tm < 250°C 2 wherein Tm is a melting point of the prepared fiber, excluding the case in which the number of melting point peaks is two or more.
Analysis of melting points was performed using a DSC 7 differential scanning calorimeter (Perkin Elmer) . If TB is lower than TFR - 20°C, the melting point difference between the base resin and the flame retardant polyester polymer is too high, thereby making it difficult to achieve uniform spinning. In contrast, if TB is higher than TFR + 20°C, incomplete melting occurs upon spinning and this then causes heterogeneous discharging resulting in frequent blow out leading to deterioration of workability, or unreacted base resin serves as a contaminant, thereby deteriorating fiber quality. In addition, if the melting point of the prepared fiber, Tm is lower than 220°C, heat resistance is lowered and thus fusion of fibers and tight spots tend to occur in post-processing. Whereas, if Tm is higher than 250°C, another melting peak is developed due to phase separation, thereby it is difficult to obtain fibers having uniform physical properties and it is difficult to prepare products having uniform colors.
Existence of two or more melting points exhibited in the prepared fibers represents a state in which two or more polymers are simply mixed without compatibility therebetween, thus resulting in ununiform distribution in the polymer melt leading to difficulty in application as fibers. Further, pigments or dyes utilized in the present invention are employed in high-temperature polyester polymerization and spinning processes and thus they should have superior heat resistance. Therefore, upon comparing and evaluating various materials on the basis of industrially reasonable costs and performance, inorganic pigments were found adequate in the present invention. In particular, carbon black was preferred. Conventional disperse dyes for polyester fibers were decomposed at a high temperature of about 280 to 300°C, thereby making it difficult to use them due to color changes .
In addition, suitable content of carbon black is between 500 and 5000 ppm, relative to the flame retardant polyester fibers. If the content of carbon black is less than 500 ppm, it is difficult to develop desired colors and it is also difficult to effect uniform blending, thereby resulting in occurrence of inferior dyeing. Whereas, if the content of carbon black is higher than 5000 ppm, the amount of carbon black added is too much, thus leading to increased production costs and deterioration of spinnability.
Although the spinning process in accordance with the present invention is a spin-draw process whereby drawing is performed in conjunction with spinning, it is also possible to perform drawing or false twisting after preparing partially oriented yarns (POY) .
[Mode for Invention]
EXAMPLES
Now, the present invention will be described in more detail with reference to the following Examples and Comparative Examples. These examples are provided only for illustrating the present invention and should not be construed as limiting the scope and spirit of the present invention.
Examples 1 through 5 and Comparative Examples 1 through 3
A slurry of 8650 g of terephthalic acid (hereinafter, referred to as "TPA") and 2700 g of ethylene glycol (hereinafter, referred to as "EG") was subjected to esterification using a semi-batch process. Oligomers prepared to have the same composition as in the slurry were stirred in an esterification reactor while the temperature of the reactor was maintained at 250 to 260°C. After completion of slurry introduction, esterification was additionally progressed for 30 minutes, thereby reaching an esterification reaction rate of 96.5%. The prepared oligomers were transferred to a polycondensation reactor. As the flame retardant, a EG solution in which the concentration of a compound of a general formula 1 (wherein p is 1, Ri and R2 are CH2CH2OH) was 65 weight % was used. 1380 g of the flame retardant solution was introduced to the reactor, and then manganese acetate and phosphoric acid, as UV stabilizers, were added to the reactor with the concentrations of 44 ppm and 75 ppm, respectively, based on manganese and phosphorus atoms. Next, as a catalyst,
200 g of a solution in which 2% by weight of antimony trioxide had been dissolved in EG was added and vacuum was applied. A conventional polyester polymerization method was used to perform polycondensation, thereby obtaining polymers having an intrinsic viscosity (IV) of
0.65 dl/g. Physical properties of the thus-prepared flame retardant polyester polymers are as follows:
Melting point: 242.8°C , Intrinsic viscosity: 0.64 dl/g, DEG: 1.30 wt%, phosphorus content: 6000 ppm,
Color: L 63, a -2.2 and b 1.0. A master batch was prepared to contain 30% by weight of carbon black using respective polymers listed in Table 1 and a twin extruder.
The prepared flame retardant polyester polymers and the master batches having the same composition as shown in Table 1 were subjected to spinning and yarn processing so as to prepare dope-dyed flame retardant polyester fibers.
Comparative Example 4 This example was carried out using the same procedure as in Example 1, except that flame retardant polyester polymers were prepared to have phosphorus content of 280 ppm.
Figure imgf000020_0001
*""" : Base resin
- PET : Polyethylene terephthalate
- PBT : Polybutylene terephthalate
- CoPET : PET copolymerized with 2.5 mol% of isophthalic acid
- PEN : Polyethylene naphthalate
*2 Master batch content : wt% of master batch upon blending (weight of master batch/ (weight of master batch + weight of flame retardant polyester polymer) x 100)
*3 Dyeability : © : no difference in dyeing, X : difference in dyeing in one or more samples, as evaluated with the naked eye, using 10 circular knitted fabrics prepared by hose knitting the prepared fibers. Separately marking for salt stain formed
*4 Two peaks in the T1n column represents occurrence of two peaks on a DSC chart
*5 Spinnability : © representing less than 3 times yarn breakages in a day spinning process; X representing 3 or more yarn breakages
*6 Flame retardancy : The prepared fibers were tested according to KS M 3032, thereby evaluating LOI (Limited Oxygen Index) . Example 6
False twist yarns of dope-dyed flame retardant polyesters prepared in Example 1 and commercially available flame retardant polyester false twist yarn, SDM 150/144 (Hyosung, Korea) , as weft and warp, respectively, were used to weave double faced satins which were then evaluated on performance as a blackout curtain. Flame retardancy of the blackout curtain was evaluated according to US standard, NFPA 701, and the blackout curtain passed the examination. In addition, shading rate of the blackout curtain was evaluated according to Japanese Standard, JIS L 1055, and was found to be 99.8%.
As described above, dope-dyed flame retardant polyester fibers in accordance with the present invention have excellent flame retardancy, UV stability and fastness. In particular, use of fibers in accordance with the present invention in preparing blackout curtains or the like can simultaneously provide excellent flame retardancy and light shieldability.
Although the preferred embodiments of the present invention have been disclosed for illustrative purposes, those skilled in the art will appreciate that various modifications, additions and substitutions are possible, without departing from the scope and spirit of the invention as disclosed in the accompanying claims .

Claims

[ CLAIMS ]
[Claim 1] A dope-dyed flame retardant polyester fiber, comprising 500 to 5000 ppm of carbon black in a flame retardant polyester polymer containing 500 to 50000 ppm of a phosphorus based flame retardant based on phosphorus atoms .
[Claim 2] The polyester fiber according to claim 1, wherein the dope-dyed flame retardant polyester fiber satisfies the following inequality 2:
220°C < Tm < 250°C 2 wherein Tm is a melting point of the prepared fiber.
[Claim 3] The polyester fiber according to claim 1, wherein the phosphorus based flame retardant is represented by the following general formula 1:
Formula 1
Figure imgf000024_0001
wherein Ri and R2 are independently hydrogen or a different or same radical having a ω -hydroxyl group and containing 2 to 4 carbon atoms, and p is an integer between 1 and 5.
[Claim 4] The polyester fiber according to claim 1, wherein the base resin of the master batch introducing carbon black into the fiber is a polyester polymer satisfying the following inequality 1:
TFR - 20°C < TB ≤ TFR + 20°C 1 wherein TFR is a melting point of the flame retardant polyester polymer and TB is a melting point of the base resin of the master batch.
[Claim 5] The polyester fiber according to claim 4, wherein the polyester polymer is selected from polyethylene terephthalate, polybutylene terephthalate, copolymerized polyethylene terephthalate containing 12 mol% or less of isophthalic acid and copolymerized polybutylene terephthalate containing 12 mol% or less of isophthalic acid.
[Claim 6] A method for preparing dope-dyed flame retardant polyester fiber, comprising adding 500 to 5000 ppm of carbon black to a flame retardant polyester polymer containing 500 to 50000 ppm of a phosphorus based flame retardant based on phosphorus atoms, using a carbon black master batch.
[Claim 7] A dope-dyed flame retardant polyester woven or knitted fabric comprising the dope-dyed flame retardant polyester fiber according to any one of claims 1 through 5.
[Claim 8] A flame retardant blackout curtain comprising the dope-dyed flame retardant polyester fiber according to any one of claims 1 through 5.
PCT/KR2005/000987 2004-12-31 2005-04-08 Dope dyed flame retardant polyester fibers, textle products therefrom and the method of manufacturing thereof WO2006070970A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
US11/792,681 US20080268736A1 (en) 2004-12-31 2005-04-08 Dope Dyed Flame Retardant Polyester Fibers, Textile Products Therefrom and the Method of Manufacturing Thereof
EP05733515A EP1831443A4 (en) 2004-12-31 2005-04-08 Dope dyed flame retardant polyester fibers, textle products therefrom and the method of manufacturing thereof
JP2007549229A JP2008525661A (en) 2004-12-31 2005-04-08 Dope dyed flame retardant polyester fibers, textile products obtained therefrom and methods for their production

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
KR1020040118132A KR100615782B1 (en) 2004-12-31 2004-12-31 Dope dyed flame retardant polyester fiber and textile products therefrom
KR10-2004-0118132 2004-12-31

Publications (1)

Publication Number Publication Date
WO2006070970A1 true WO2006070970A1 (en) 2006-07-06

Family

ID=36615065

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/KR2005/000987 WO2006070970A1 (en) 2004-12-31 2005-04-08 Dope dyed flame retardant polyester fibers, textle products therefrom and the method of manufacturing thereof

Country Status (7)

Country Link
US (1) US20080268736A1 (en)
EP (1) EP1831443A4 (en)
JP (1) JP2008525661A (en)
KR (1) KR100615782B1 (en)
CN (1) CN100552103C (en)
TW (1) TWI363817B (en)
WO (1) WO2006070970A1 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008174890A (en) * 2006-11-22 2008-07-31 Hyosung Corp Flame-retardant dope-dyed polyester fiber, and fabric and blackout cloth produced therefrom
EP1961846A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
EP1961844A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
EP1961845A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
ITMI20090723A1 (en) * 2009-04-28 2010-10-29 Filatura Di Pray Di Barberis Canoni Co Marco & Co METHOD AND INTERMEDIATE PRODUCT TO MAKE A THREAD OR FABRIC WITH DELAYED INFLAMMABILITY AND THE THREAD OR FABRIC SO IT IS OBTAINED
CN105063793A (en) * 2015-08-07 2015-11-18 无锡双象超纤材料股份有限公司 Super-fine denier flame-retardant polyurethane short fiber and preparation method thereof

Families Citing this family (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100856869B1 (en) * 2008-03-17 2008-09-04 김인효 Fire resistance fabrics
KR101016124B1 (en) 2008-11-14 2011-02-17 한국염색기술연구소 The resist printing reserve printing stretch manufacture through bath-method made-up yarn dyeing or flame retardant finish and resist printing reserve printing stretch fabric manufacture method
KR101317606B1 (en) 2008-12-30 2013-10-10 코오롱인더스트리 주식회사 Polyester spun dyed yarn and preparation method thereof
KR101041159B1 (en) 2010-12-06 2011-06-13 유진섬유 주식회사 Heat-melted fiber with excellent flame-retardant and light-shielding characteristic and textile goods using the same
CN102199807B (en) * 2011-03-29 2012-07-04 浙江古纤道新材料股份有限公司 Method for producing phosphorus copolymerized flame-retarding terylene high-strength industrial yarns
CN103122543A (en) * 2011-11-18 2013-05-29 东丽纤维研究所(中国)有限公司 Flame resistant textile and application thereof
CN102628194B (en) * 2012-03-23 2013-11-06 台州东海塑料品制造有限公司 Terylene air-jet textured yarn fabric with high color fastness
CN103074702B (en) * 2013-01-22 2015-04-01 中国人民解放军总后勤部军需装备研究所 Flame retardant polyester fiber as well as preparation method and application thereof
TWI475100B (en) * 2013-05-29 2015-03-01 Sino Japan Chemical Co Ltd Water-soluble flame retardant composition and application thereof
CN103382598A (en) * 2013-07-30 2013-11-06 常熟市新达纬编厂 Preparing method of composite aramid fiber aerial flame-retardant fabrics
CN104140648B (en) * 2014-07-17 2016-01-20 滁州优胜高分子材料有限公司 A kind of permanent fire retardant PBT material
CN104983100B (en) * 2015-06-29 2016-08-24 安徽东锦服饰有限公司 Water proof fire retardant functional clothing fabric processing method
CN112281278B (en) * 2020-10-15 2023-03-17 绍兴三立达纺织阻燃新材料有限公司 Flame-retardant polyester rolling curtain fabric and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08322707A (en) * 1995-06-01 1996-12-10 Teijin Ltd Flame-proof blackout curtain
JP2001279073A (en) * 2000-03-31 2001-10-10 Takagi Chemicals Inc Flame-retardant polyester resin composition, flame- retardant polyester fiber, method of producing the flame retardant and flame-retardant polyester fiber
WO2003071014A1 (en) * 2002-02-22 2003-08-28 Kaneka Corporation Flame-retardant polyester fiber and artificial hair comprising the same

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2346787C3 (en) * 1973-09-17 1980-05-08 Hoechst Ag, 6000 Frankfurt Flame retardant linear polyesters, processes for their manufacture and their use
JPS5922717B2 (en) * 1976-02-13 1984-05-28 東洋紡績株式会社 Novel organophosphorus compound
JPS6399375A (en) * 1986-10-13 1988-04-30 帝人株式会社 Flameproof black raw yarn
US5180793A (en) * 1991-12-31 1993-01-19 Hoechst Celanese Corporation Flame resistant, low pilling polyester fiber
KR960701122A (en) * 1993-02-22 1996-02-24 나가따 마사오 FLAME RETARDANT POLYESTER
US5530088A (en) * 1995-06-21 1996-06-25 Industrial Technology Research Institute Heat resistant phosphorus-containing polymeric flame retardant and process for preparing the same
JPH0949143A (en) * 1995-08-02 1997-02-18 Nippon Ester Co Ltd Noncoating mesh coat
US5899428A (en) * 1996-06-06 1999-05-04 Lear Corporation Vehicle power seat adjuster with self-locking track assemblies
JP2001073251A (en) * 1999-08-30 2001-03-21 Toyobo Co Ltd Polyester textile excellent in flame retardance
US6740276B2 (en) * 2001-06-29 2004-05-25 E. I. Du Pont De Nemours And Company Process for preparing pigmented shaped articles comprising poly (trimethylene terephthalate)
KR20040017283A (en) * 2001-07-19 2004-02-26 가네가후치 가가쿠 고교 가부시키가이샤 Polyester based fiber and artificial hair using the same
DE60302938T2 (en) * 2002-06-12 2006-09-21 KURARAY CO., LTD, Kurashiki Flame resistant, leathery sheet substrate and method of making the same

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08322707A (en) * 1995-06-01 1996-12-10 Teijin Ltd Flame-proof blackout curtain
JP2001279073A (en) * 2000-03-31 2001-10-10 Takagi Chemicals Inc Flame-retardant polyester resin composition, flame- retardant polyester fiber, method of producing the flame retardant and flame-retardant polyester fiber
WO2003071014A1 (en) * 2002-02-22 2003-08-28 Kaneka Corporation Flame-retardant polyester fiber and artificial hair comprising the same

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP1831443A4 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008174890A (en) * 2006-11-22 2008-07-31 Hyosung Corp Flame-retardant dope-dyed polyester fiber, and fabric and blackout cloth produced therefrom
EP1961846A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
EP1961844A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
EP1961845A3 (en) * 2007-02-24 2009-09-02 Teijin Monofilament Germany GmbH Electrically conductive filaments, fabrics made of these filaments and their use
ITMI20090723A1 (en) * 2009-04-28 2010-10-29 Filatura Di Pray Di Barberis Canoni Co Marco & Co METHOD AND INTERMEDIATE PRODUCT TO MAKE A THREAD OR FABRIC WITH DELAYED INFLAMMABILITY AND THE THREAD OR FABRIC SO IT IS OBTAINED
CN105063793A (en) * 2015-08-07 2015-11-18 无锡双象超纤材料股份有限公司 Super-fine denier flame-retardant polyurethane short fiber and preparation method thereof

Also Published As

Publication number Publication date
TW200622048A (en) 2006-07-01
CN101084331A (en) 2007-12-05
CN100552103C (en) 2009-10-21
EP1831443A1 (en) 2007-09-12
TWI363817B (en) 2012-05-11
KR20060078795A (en) 2006-07-05
JP2008525661A (en) 2008-07-17
US20080268736A1 (en) 2008-10-30
EP1831443A4 (en) 2009-08-26
KR100615782B1 (en) 2006-08-25

Similar Documents

Publication Publication Date Title
US20080268736A1 (en) Dope Dyed Flame Retardant Polyester Fibers, Textile Products Therefrom and the Method of Manufacturing Thereof
KR101739402B1 (en) Copolyester and preparation method and use thereof
US7776945B2 (en) Polyester fiber having excellent light-shielding and flame retardant characteristic and textile goods using the same
JP2005320533A (en) Cationic dye-dyeable and flame-retardant polyester polymer and its manufacturing method
EP0550034B1 (en) Flame resistant, low pilling polyester fiber
KR20070039494A (en) Polytrimethylene terephthalate
JP2008174890A (en) Flame-retardant dope-dyed polyester fiber, and fabric and blackout cloth produced therefrom
JPH05230345A (en) Flame-resistant polyester
DE102008046383A1 (en) Flame retardant with cationic dye of colorable copolyester polymer, useful to prepare cationic dye of colorable copolyester fiber, comprises a metal sulfonate compound, and a flame protecting agent based on phosphorous compound
JP5912669B2 (en) Cationic dye-dyeable flame retardant polyester fiber and its fiber products
KR100449383B1 (en) Manufacturing method of fire retardant polyester fiber having excellent mechanical properties
JPH08269850A (en) Net and mesh for building material
JP2010059572A (en) Atmospheric cation dyeable polyester conjugate fiber
US4045513A (en) Ethylene 2,6-naphthalene dicarboxylated-alkylene-2,5 dibromoterephthalate flame-retardant copolyesters
US20190292690A1 (en) Semi-crystalline thermoplastic polyester for producing fibres
JP5216972B2 (en) Method for producing atmospheric pressure cationic dyeable polyester fiber
KR100526051B1 (en) A process for preparing ultrafine polyester fibers having excellent flame retardancy
JP5216971B2 (en) Method for producing cationic dyeable polyester fiber
KR100341940B1 (en) Manufacturing process of nonflammable polyester
JP2008174861A (en) Cation-dyeable ultrafine polyester combined filament yarn
CA1081896A (en) Copolyesters derived from ethoxylated 3,5-dibromo-4- hydroxybenzoic acid
EP1493853B1 (en) Modified polyester fiber and process for producing the same
CN116234853A (en) Polyester resin for preparing CD-PET and CD-PET composite resin containing same
JP2010280862A (en) Cation dyeable polyether ester block copolymer and fiber
GB1578810A (en) Flame-retardant copolyester

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
DPE2 Request for preliminary examination filed before expiration of 19th month from priority date (pct application filed from 20040101)
WWE Wipo information: entry into national phase

Ref document number: 2005733515

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 200580043775.6

Country of ref document: CN

WWE Wipo information: entry into national phase

Ref document number: 2007549229

Country of ref document: JP

NENP Non-entry into the national phase

Ref country code: DE

WWP Wipo information: published in national office

Ref document number: 2005733515

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 11792681

Country of ref document: US