US20050159552A1 - Flame retarded fibers and filaments and process of production therefor - Google Patents

Flame retarded fibers and filaments and process of production therefor Download PDF

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Publication number
US20050159552A1
US20050159552A1 US10/762,787 US76278704A US2005159552A1 US 20050159552 A1 US20050159552 A1 US 20050159552A1 US 76278704 A US76278704 A US 76278704A US 2005159552 A1 US2005159552 A1 US 2005159552A1
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United States
Prior art keywords
fiber
styrenic polymer
anionic styrenic
polybrominated anionic
polymer
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Abandoned
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US10/762,787
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English (en)
Inventor
Jon Reed
Daniel De Schryver
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Albemarle Corp
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Albemarle Corp
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Priority to US10/762,787 priority Critical patent/US20050159552A1/en
Priority to CA2552434A priority patent/CA2552434C/en
Priority to AU2004317802A priority patent/AU2004317802A1/en
Priority to SG201006183-6A priority patent/SG165312A1/en
Priority to RU2006129939/04A priority patent/RU2006129939A/ru
Priority to BRPI0418453-0A priority patent/BRPI0418453A/pt
Priority to ES04821608T priority patent/ES2402050T3/es
Priority to KR1020067014367A priority patent/KR101225265B1/ko
Priority to CN200480040827XA priority patent/CN101166852B/zh
Priority to PCT/US2004/033756 priority patent/WO2005095685A1/en
Priority to JP2006551045A priority patent/JP4767866B2/ja
Priority to EP04821608A priority patent/EP1706525B1/en
Priority to PL04821608T priority patent/PL1706525T3/pl
Publication of US20050159552A1 publication Critical patent/US20050159552A1/en
Priority to IL176956A priority patent/IL176956A/en
Priority to US11/490,300 priority patent/US7666943B2/en
Assigned to ALBEMARLE CORPORATION reassignment ALBEMARLE CORPORATION ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: REED, JON SHANNON, DE SCHRYVER, DANIEL A.
Priority to US11/928,900 priority patent/US7666944B2/en
Abandoned legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F1/00—General methods for the manufacture of artificial filaments or the like
    • D01F1/02—Addition of substances to the spinning solution or to the melt
    • D01F1/07—Addition of substances to the spinning solution or to the melt for making fire- or flame-proof filaments
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02—Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10—Homopolymers or copolymers of propene
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L67/00—Compositions of polyesters obtained by reactions forming a carboxylic ester link in the main chain; Compositions of derivatives of such polymers
    • C08L67/02—Polyesters derived from dicarboxylic acids and dihydroxy compounds
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/02—Polyamides derived from omega-amino carboxylic acids or from lactams thereof
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00—Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers
    • C08L77/06—Polyamides derived from polyamines and polycarboxylic acids
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D01F6/04—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins
    • D01F6/06—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polyolefins from polypropylene
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/46—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polyolefins
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/44—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/48—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds as major constituent with other polymers or low-molecular-weight compounds of polymers of halogenated hydrocarbons
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/60—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyamides
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/58—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products
    • D01F6/62—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolycondensation products from polyesters
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/90—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyamides
    • D—TEXTILES; PAPER
    • D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
    • D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
    • D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
    • D01F6/88—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds
    • D01F6/92—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from mixtures of polycondensation products as major constituent with other polymers or low-molecular-weight compounds of polyesters
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00—Use of inorganic substances as compounding ingredients
    • C08K3/01—Use of inorganic substances as compounding ingredients characterized by their specific function
    • C08K3/016—Flame-proofing or flame-retarding additives
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L25/00—Compositions of, homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Compositions of derivatives of such polymers
    • C08L25/18—Homopolymers or copolymers of aromatic monomers containing elements other than carbon and hydrogen

Definitions

  • thermoplastic fibers and filaments including those where the thermoplastic is a polyester, polyamide, polyolefin, or an acrylic, which are flame-retarded with a brominated styrenic polymer.
  • flame retardant additives tend to form nonuniform distributions in the mixture, and thus result in nonhomogeneous flame-retarded fibers, which have poor mechanical properties.
  • the problems associated with nonhomogeneity are more pronounced for finer fibers.
  • the flame retardant additive if the flame retardant additive is not completely mixed with the synthetic fiber material prior to extrusion, the flame retardant additive tends to agglomerate onto itself, producing lumps in the extrusion melt, clogging the spinneret filters or orifices, or producing weak spots in the resulting continuous filament. Such agglomerated lumps also necessarily produce other areas in which there will be a lack of flame retardant additive, and thus reduced flame retardant effectiveness.
  • brominated polystyrenes have oftentimes been deficient in their color characteristics.
  • Manufacturers of products containing flame retardants generally find it advantageous to have available a flame retardant which will not contribute excessive color to the products or otherwise interfere with color matching specifications applicable to a given product.
  • the lower the color of the brominated styrenic polymer i.e., the whiter the flame retardant
  • high-melting flame retardants that are white often end up acting as a white pigment in the fiber, making coloring the fibers more difficult, as the white color of the flame retardant must be overcome.
  • Polybrominated anionic styrenic polymers are compatible with, and provide flame retardancy to, fiber-forming thermoplastic polymers. Such flame retardants have lower viscosities and greater thermal stability than polybrominated non-anionic styrenic polymers, an advantage in processes such as melt blending and fiber spinning. Due to their compatibility with fiber-forming thermoplastic polymers, the introduction of polybrominated anionic styrenic polymers at the formation stage of fibers and filaments eliminates the need for later processing to flame retard a fabric, and the flame retardancy imparted by the intimate mixture of the polybrominated anionic styrenic polymer with a fiber-forming thermoplastic polymer is expected to be relatively permanent, unlike a coating.
  • polybrominated anionic styrenic polymers form relatively uniform mixtures and thus result in more homogeneous fibers. Because of the greater homogeneity, it is also possible to obtain finer (thinner) fibers which contain a flame retardant and still retain good mechanical properties. Other advantages of the greater homogeneity are that the mixtures are far less likely to clog spinneret orifices, and the produced fibers or filaments will have few areas in which the flame retardant is absent.
  • polybrominated anionic styrenic polymers have been found to exhibit minimal color development.
  • the use of a polybrominated anionic styrenic polymer with a polyamide enables a reduction of color formation.
  • polybrominated anionic styrenic polymers are present even when the bromine content of the anionic styrenic polymer is 67 wt % or more. Further, these polybrominated anionic styrenic polymers release minimal amounts of hydrogen halide under thermal processing conditions, thereby greatly reducing the opportunity for corrosion of processing equipment to occur during polymer processing operations.
  • One embodiment of the invention is a fiber or filament formed from ingredients comprising (a) at least one fiber-forming thermoplastic polymer, and (b) at least one polybrominated anionic styrenic polymer.
  • the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %.
  • Another embodiment of the invention is a process for producing a fiber or filament, which process comprises melt spinning (a) at least one fiber-forming thermoplastic polymer, and (b) at least one polybrominated anionic styrenic polymer.
  • the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %.
  • composition which is a carrier blend.
  • the blend is formed from ingredients comprising (i) at least one polybrominated anionic styrenic polymer, wherein the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %, and (ii) at least one synergist or at least one other flame retardant.
  • Yet another embodiment of the invention is a process for forming a carrier blend. This process comprises mixing and melting together (i) at least one polybrominated anionic styrenic polymer, wherein the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %, and (ii) at least one synergist or at least one other flame retardant.
  • Another embodiment of the invention is a process for producing a fiber or filament, which process comprises melt spinning (a) at least one fiber-forming thermoplastic polymer, and (b) a carrier blend of this invention.
  • the flame retardants, the polybrominated anionic styrenic polymers used in this invention, are brominated styrenic polymers, preferably a brominated anionic polystyrene. These polybrominated anionic styrenic polymers have a bromine content of at least about 50 wt %, preferably at least about 60 wt %, and more preferably at least about 67 wt %. All wt % and ppm levels in reference to the polybrominated anionic styrenic polymers are based on the total weight of the brominated styrenic polymer, unless otherwise stated.
  • the low molecular weight of the polybrominated anionic styrenic polymer leads to better compatibility with the fiber-forming polymer, and thus better blending, as well as more homogenous distribution of the flame retardant, giving a more uniform mixture, which results in fibers and filaments that are more uniform.
  • the melt-blendable nature of low molecular weight brominated anionic polystyrene minimizes interference on color matching. This is advantageous in that less pigment needs to be added to the fibers to achieve the desired color.
  • the polybrominated anionic styrenic polymer is generally at least about 2 wt % of the fiber or filament.
  • the polybrominated anionic styrenic polymer is within the range of from about 5 to about 20 wt %, the wt % being based on the total weight of the fiber or filament.
  • Other ingredients may also be present in the fiber or filament.
  • flame retardant synergists are often used. The amount of flame retardant synergist, when used, generally will be in the range of up to about 12 wt % based on the total weight of the finished fiber or filament.
  • a preferred fiber or filament of the invention has about 93-97 wt % fiber-forming polymer, about 2-5 wt % polybrominated anionic styrenic polymer, and about 1-2 wt % of another ingredient, particularly a synergist.
  • Another preferred fiber or filament has about 96-98 wt % fiber-forming polymer and about 2-4 wt % polybrominated anionic polystyrene.
  • nylon fiber containing brominated anionic polystyrene was formed, and illustrates the beneficial qualities imparted to a fiber or filament of the invention.
  • This inventive nylon fiber had decreased water uptake in comparison to neat nylon fiber (well-known in the art for its high water uptake). A result of the decreased water uptake was an increase in fiber stiffness and improved dimensional stability. Further, the domain size of brominated anionic polystyrene in some nylons is very small, as measured by scanning electron microscopy (SEM).
  • the fiber-forming polymers in the compositions of the invention are thermoplastic, and include polyesters, polyamides (nylons), polyolefins, acrylates, and mixtures of such thermoplastics. Polyesters and polyamides are preferred types of fiber-forming thermoplastic polymers.
  • Thermoplastic polyesters are reaction products of a dicarboxylic acid together with a diol and/or a hydroxy carboxylic acid; the self-condensation of a hydroxy carboxylic acid; or mixtures of such reaction products.
  • Reactive derivatives of dicarboxylic acids such as methyl esters or anhydrides, may also be used.
  • Related copolyesters and blends including blends of one or more thermoplastic polyesters with one or more other thermoplastic polymers such as polycarbonates, are included as fiber-forming thermoplastic polymers that can be used in the compositions of the invention.
  • Dicarboxylic acids which can be used in the formation of polyesters include aliphatic dicarboxylic acid having 2-20 carbon atoms such as azelaic acid, adipic acid, sebacic acid, and dodecanedicarboxylic acid; alicyclic dicarboxylic acids such as cyclopentanedicarboxylic acid and cyclohexanedicarboxylic acid; and aromatic dicarboxylic acids such as terephthalic acid, isophthalic acid, orthophthalic acid, hydroxybenzoic acid, hydroxynaphthoic acid, diphenylenehydroxycarboxylic acid, naphthalene-dicarboxylic acid, and the like.
  • Alkyl and/or alkoxy substituted derivatives of these acids may also be used.
  • These dicarboxylic acids may be each used in the form of their ester-forming derivatives, such as dimethyl esters. Mixtures of two or more of the foregoing dicarboxylic acids (and/or their ester-forming derivatives) can be used.
  • Diols that can be used to form polyesters include, but are not limited to, ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,4-butanediol, 2,3-butanediol, 1,5-pentanediol, neopentyl glycol, 1,6-hexanediol, 1,10-decanediol, 1,3-cyclohexanediol, 1,4-cyclohexanediol, 1,4-bishydroxymethylcyclohexane, hydroquinone, resorcinol, catechol, napthalenediol, dihydroxydiphenyl ether, 2,2-bis(4-hydroxyphenyl)propane and diethoxylated bisphenol A. Alkyl and/or alkoxy substituted derivatives of these diols also may be used. Mixtures of two or more of the foregoing diols also may be suitable for use.
  • the polyester to be used in the present invention also may be a polyester having a branched or crosslinked structure which is prepared by using a minor amount of a trifunctional monomer in addition to the above components.
  • Preferred trifunctional monomers include trimellitic, trimesic and pyromellitic acids, pentaerythritol and trimethylolpropane. Mixtures of two or more polyesters may be used.
  • Preferred polyesters in this invention are polyethylene terephthalate, polybutylene terephthalate, or polytrimethylene terephthalate. More preferred are polyethylene terephthalate and polybutylene terephthalate.
  • Polyalkylene terephthalates may be produced by known methods. See, for example, Encyclopedia of Polymer Science and Technology , Vol. 11, pages 62-128, John Wiley & Sons, Inc., copyright 1969; and Kirk-Othmer, Encyclopedia of Chemical Technology, 4th Ed., Vol. 19, pages 609-653, John Wiley & Sons, Inc., copyright 1996.
  • the polyamide thermoplastic fiber-forming polymer can be any amorphous and/or partly crystalline, predominately aliphatic/cycloaliphatic or partially aromatic thermoplastic polyamide. Typically such materials are produced by polycondensation and/or polymerization processes from diamines which are predominately or entirely aliphatic or cycloaliphatic, or which are partially or entirely aromatic, and dicarboxylic acids or lactams which are predominantly or entirely aliphatic or cycloaliphatic, or which are partially or entirely aromatic.
  • Typical amines used in forming polyamides include such diamines as hexamethylenediamine, tetramethylenediamine, 2,2,4- and 2,4,4-trimethylhexa-methylene-diamine, diaminobutane, diaminodicyclohexylmethane, diaminodicyclohexylpropane, and isophoronediamine, and xylylenediamine.
  • Lactams with at least six carbon atoms in the ring may be used; such lactams include caprolactam, 4-tert-butylcaprolactam, 2-azacyclooctanone (enantholactam), 2-azacyclononanone, and lauryllactam (dodecanolactam).
  • lactams include caprolactam, 4-tert-butylcaprolactam, 2-azacyclooctanone (enantholactam), 2-azacyclononanone, and lauryllactam (dodecanolactam).
  • aminocarboxylic acids such as ⁇ -aminocaproic acid, or ( ⁇ -aminocarboxylic acids such as ⁇ -aminolauric acid and ⁇ -aminoundecanoic acid.
  • the carboxylic acid used are aliphatic or mixed aliphatic-aromatic dicarboxylic acids having less than 50% by weight aromatic constituents such as adipic acid, 2,2,4- and 2,4,4-trimethyladipic acid, azelaic acid, sebacic acid, decanedicarboxylic acid, dodecanedicarboxylic acid, cyclohexanedicarboxylic acid, hexahydroterephthalic acid, isophthalic acid and terephthalic acid.
  • Copolyamides from the majority of the known monomers can also be used.
  • Illustrative polyamides which may be used in the practice of this invention are such polyamides as nylon-6 (polycaprolactam), nylon-6,6 (from hexamethylenediamine and adipic acid), nylon-6,9, nylon-6,10 (from hexamethylenediamine and sebacic acid), nylon-6,12, nylon-11 (polyundecanolactam), nylon-12 (polylauryllactam), nylon-12,12, nylon-6/66 (poly(hexamethylene adipamide-co-caprolactam)), and high temperature nylons, particularly aromatic polyamides and partially aromatic polyamides.
  • nylons examples include nylon-4,6 (from diaminobutane and adipic acid), and partially aromatic nylons (e.g., Ixef polyarylamide PA MXD6 from Solvay, Zytel HTN from DuPont, and Amodel polyarylamide from BP-Amoco or Grivory HT or HT1 or HT2 from Ems-Chemie or Arlen polyarylamide from Mitsui or Genestar 9T from Kuraray).
  • Other polyamides which may be used include Stanyl polyamide 46 from DSM, Vydyne polyamide 6/66 copolymers from Dow/Solutia, polyamide 612 (Vestamid D from Creanova), and similar polyamides.
  • thermoplastic blends or alloys of one or more polyamides with one or more other thermoplastic polymers such as, for example, polyamide-polyolefin blends or alloys. Mixtures of two or more polyamides may also be used.
  • thermoplastic fiber-forming polyolefins include homopolymers and copolymers of olefins such as ethylene, propylene, 1-butene, 1-pentene, 1-hexene, 1-heptene, 1-octene, and the like.
  • Such polyolefins include, but are not limited to, polyethylene, including low-molecular-weight polyethylene, polypropylene, including low-molecular-weight polypropylene, ethylene-polypropylene copolymers, ethylene-1-butene copolymer, ethylene-1-hexene copolymers, and ethylene-1-octene copolymers.
  • polyolefins in which at least 50 percent by weight is formed from propylene are also deemed suitable for use in this invention.
  • Copolymers of propylene that may be used include copolymers with one or more alpha-olefins such as ethylene, 1-butene, 1-pentene, 3-methyl-1-butene, and analogous alpha-olefins.
  • Suitable polyolefin copolymers include ethylene-vinyl acetate copolymer, ethylene-methylmethacrylate copolymer, ethylene-ethyl acrylate copolymer, ethylene-acrylic acid copolymer, ethylene-vinyl alcohol copolymer, and like ethylene copolymers, and the like.
  • Mixtures of two or more of the foregoing olefin polymers and/or copolymers may also be used. Mixtures of polyolefins with one or more polyamides and/or one or more polyesters can also be used in the compositions of the invention.
  • the fiber-forming thermoplastic polymer in this invention includes acrylics, which are homopolymers and copolymers of unsaturated carboxylic acids and their alkyl esters such as acrylic acid, methacrylic acid, methylacrylate, methylmethacrylate, ethyl acrylate, butyl acrylate, ethylene glycol diacrylate, ethylene glycol dimethacrylate, diethylene glycol diacrylate, diethylene glycol dimethacrylate, triethylene glycol diacrylate, triethylene glycol dimethacrylate, 1,3-butylene glycol diacrylate, 1,3-butylene glycol dimethacrylate, 1,4-butylene glycol dimethacrylate, 1,6-hexane glycol diacrylate, 1,6-hexane glycol dimethacrylate, neopentyl glycol diacrylate, neopentyl glycol dimethacrylate, trimethylol propane triacrylate, trimethylol propane trimethacrylate, trimethylol
  • Blends or alloys of one or more acrylics with one or more of the other types of thermoplastic fiber-forming polymers may also be used.
  • a polybrominated anionic styrenic polymer is an anionic styrenic polymer that has been brominated such that the bromine content of the polymer is at least about 50 wt % of the polymer, preferably at least about 60 wt %, and more preferably at least about 67 wt % of the polymer.
  • the polybrominated anionic styrenic polymer functions as a flame retardant in the fiber and filament compositions of the invention.
  • the brominated styrenic polymers (preferably brominated anionic polystyrenes) used in this invention possess certain additional important properties or characteristics. These properties or characteristics pertain to such factors as thermal stability, very low ⁇ E color values measured using 10 wt % solutions in chlorobenzene, desirable melt flow indices, desirable GPC number average molecular weights, and total chlorine content (if any).
  • the above polybrominated anionic styrenic polymer used in this invention is preferably a brominated anionic polystyrene.
  • a particularly preferred polybrominated anionic polystyrene is a polybrominated anionic polystyrene having a typical bromine content of approximately 68 wt % formed from anionic polystyrene. This product is available from Albemarle Corporation under the trade designation SAYTEX® HP-3010. Polybrominated anionic polystyrenes and their preparation are described for example in U.S. Pat. No. 6,521,714, issued Feb. 18, 2003, WO 02/072645, published Sep. 19, 2002, and U.S. application Ser. No. 10/211,648, filed Aug. 1, 2002.
  • Styrenic polymers which are brominated to form the polybrominated anionic styrenic polymers of this invention are homopolymers and copolymers of vinyl aromatic monomers.
  • Preferred vinyl aromatic monomers have the formula: H 2 C ⁇ CR—Ar wherein R is a hydrogen atom or an alkyl group having from 1 to 4 carbon atoms and Ar is an aromatic group (including alkyl-ring substituted aromatic groups) of from 6 to 10 carbon atoms.
  • Examples of such monomers are styrene, alpha-methylstyrene, ortho-methylstyrene, meta-methylstyrene, para-methylstyrene, para-ethylstyrene, isopropenyltoluene, vinylnaphthalene, isopropenylnaphthalene, vinylbiphenyl, vinylanthracene, the dimethylstyrenes, ethyl-alpha-methylstyrene, propylstyrene, tert-butylstyrene, the several bromostyrenes (such as the monobromo-, dibromo-, and tribromo- variants).
  • Styrenic polymers include, for example, polystyrene, poly-a-methylstyrene, polyvinyltoluene, styrene-a-methylstyrene copolymers and the like.
  • Polystyrene is the preferred anionic styrenic polymer.
  • styrene be one of the monomers and that styrene comprise at least 50 weight percent of the copolymerizable vinyl aromatic monomers.
  • the initial bromostyrenic polymer must have a lower bromine content than the bromine content to be present in the brominated styrenic polymer of this invention.
  • brominated styrenic polymer refers to a brominated polymer produced by bromination of a pre-existing styrenic polymer such as polystyrene or a copolymer of styrene and at least one other vinyl aromatic monomer, as distinguished from an oligomer or polymer produced by oligomerization or polymerization of one or more brominated styrenic monomers, the properties of the latter oligomers or polymers being considerably different from brominated anionic polystyrene in a number of respects.
  • the styrenic polymers used in the production of the brominated styrenic polymers which are used as flame retardants in this invention are produced by anionically-initiated polymerization. See U.S. Pat. Nos. 5,902,865, 5,717,040, 4,883,846, and 4,442,273 for descriptions of methods for anionic polymerization of vinyl aromatic monomers. As is known in the art, anionic polymerization of styrenic monomers has very high monomer conversion, and also results in monodisperse product polymer.
  • the polystyrene used to produce the brominated anionic polystyrenes of this invention will typically have a M w within the range of from about 500 to about 500,000 and a polydispersity within the range of from at least about 1 to about 4. It is desirable to conduct the bromination of the styrenic polymer using anionic styrenic polymers such as anionic polystyrene having GPC weight average molecular weights in the range of about 500 to about 15,000, preferably in the range of about 1000 to about 10,000, and more preferably in the range of about 2000 to about 8000.
  • a particularly preferred process for preparing anionic styrenic polymers comprises:
  • the liquid saturated hydrocarbon diluent in this particularly preferred process for preparing anionic styrenic polymers may be any aliphatic or cycloaliphatic hydrocarbon, or a mixture of two or more of the same, which is liquid under reaction conditions.
  • the saturated hydrocarbon preferably contains in the range of about 4 to about 12 carbon atoms in the molecule, and the aliphatic hydrocarbon may be linear or branched.
  • suitable aliphatic hydrocarbons include pentane, isopentane, hexane, 2-methylpentane, octane, 2,2,4-trimethylpentane and the like. More preferably, the liquid saturated hydrocarbon is one or more liquid saturated cycloaliphatic hydrocarbons.
  • Suitable non-limiting examples of such cycloaliphatic hydrocarbons are cyclopentane, methylcyclopentane, cyclohexane, methylcyclohexane, cycloheptane, 1,3-dimethylcyclohexane, 1,4-dimethylcyclohexane and the like, with cyclohexane being particularly preferred as the liquid saturated hydrocarbon diluent.
  • the ether promoter in this particularly preferred process for preparing anionic styrenic polymers may be a saturated aliphatic or cycloaliphatic monoether, a saturated aliphatic or cycloaliphatic diether or an aromatic ether.
  • suitable ether promoters include tetrahydrofuran, methyl tert-butyl ether, ethyl tert-butyl ether, 1,4 dioxane, dimethoxyethane, methoxybenzene, and the like.
  • the ether promoter is preferably a saturated cyclic or acyclic monoether having in the range of 4 to about 8 carbon atoms in the molecule.
  • the monoether is tetrahydrofuran (sometimes also referred to herein as “THF”), methyltetrahydrofuran or dimethyltetrahydrofuran, or a mixture of any two or more of these. Tetrahydrofuran is particularly preferred.
  • the monoether consists essentially of an alkyl tert-butyl ether.
  • Suitable alkyl tert-butyl ethers include, e.g., linear and branched chain alkyl tert-butyl ethers such as, e.g., methyl tert-butyl ether (sometimes also referred to herein as “MTBE”) and ethyl tert-butyl ether, with methyl tert-butyl ether being particularly preferred. It is desirable to use an ether that is a liquid under the reaction conditions being used.
  • the organolithium initiator may be one of many lithium-containing hydrocarbons. Suitable non-limiting examples include methyllithium, ethyllithium, —or sec-butyllithium, isopropyllithium, cyclohexyllithium or phenyllithium, including mixtures of the foregoing. n-Butyllithium and sec-butyllithium are preferred, with n-butyllithium being particularly preferred.
  • the organolithium initiator is used in solution with a saturated hydrocarbon which may be the same or different from the liquid saturated hydrocarbon diluent, but is preferably the same.
  • Prefeeding a portion of the styrenic monomer is not required for all variations of this particularly preferred process for preparing anionic styrenic polymers, but is preferred because it appears to reduce the likelihood of reaction between the ether promoter and the organolithium initiator.
  • the portion of the styrenic monomer which is prefed can vary, but typically will be about 1 percent by weight of the total amount of the styrenic monomer to be used in carrying out the reaction.
  • the feeds are maintained to provide preferably in the range of about 1 to about 10 mol %, more preferably about 2 to about 5 mol %, and most preferably in the range of about 2.5 to about 3.5 mol % of organolithium initiator based on the total amount of the styrenic monomer.
  • the feed rate of the organolithium feed is preferably about 2 to about 10 minutes, more preferably about 5 minutes, and the styrene co-feed should be effected in no more than about 2 hours, and more preferably within about 90 minutes or less, measured from initiation of co-feeding.
  • the styrene monomer co-feed preferably continues for a period of time not exceeding about 5 hours measured from initiation of the concurrent feeds.
  • the reactor used in this particularly preferred process for preparing anionic styrenic polymers is typically equipped with a overhead heat exchanger.
  • the process may be conducted at sub-atmospheric, atmospheric or super-atmospheric pressure. However, it is preferred to carry out the reaction at a reduced pressure, e.g., in the range from about 0.1 to about 0.7 atmospheres, so that the solvent is refluxed thereby providing consequent evaporative cooling of the highly exothermic reaction.
  • the process is preferably conducted in the absence of oxygen.
  • the process should be carried out under an inert atmosphere such as, e.g., nitrogen or argon.
  • the reaction system should be essentially anhydrous. By this is meant that small amounts of water insufficient to destroy the organolithium catalyst can be tolerated, but from a practical standpoint, the reaction equipment and reaction mixture should be kept as dry as reasonably practicable.
  • the temperature of the resultant reaction mixture in this particularly preferred process for preparing anionic styrenic polymers is maintained at or below the specified temperature of about 55° C. by any known method.
  • the reactor in which the reaction is conducted can be equipped with an external, indirect heat exchanger with a pump-around loop.
  • the heat exchanger itself can be provided with a suitable coolant, e.g., a glycol coolant.
  • the reaction mixture is maintained at a temperature in the range of about 25° C. to about 50° C.
  • the reaction mixture typically is held at the reaction temperature for about 5-10 minutes, e.g., when employing a scale of 3000-6000 lbs.
  • the aqueous phase which results is separated and the polymer-containing organic phase is devolatilized of the ether promoter and saturated hydrocarbon.
  • Devolatization can be carried out in a variety of ways, including for example by pre-heating the mixture in a heat exchanger and feeding it into a hot (200° C.) column under conditions such that the residual solvent and promoter are less than 0.5% by weight of the isolated polymer existing at the bottom of the column.
  • the remaining polymer may then be dissolved in a suitable solvent, e.g., bromochloromethane, for storage.
  • a suitable solvent e.g., bromochloromethane
  • Another way of terminating the reaction is to employ a lower alkyl halide, typically an alkyl chloride or an alkyl bromide, having in the range of 1 to about 8 carbon atoms.
  • an alkyl halide results in the formation of a styrenic polymer substantially all of which has one of its end groups terminated by an alkyl group rather than a proton.
  • a stoichiometric amount relative to the organolithium, should be employed.
  • a feature of this termination method is that the reaction product can remain substantially anhydrous since no water is added during production.
  • the amount of saturated hydrocarbon diluent and ether promoter employed in this particularly preferred process for preparing anionic styrenic polymers may vary, but preferably is sufficient in the aggregate to cause the resultant reaction mixture to contain about 5 to about 70 wt %, and more preferably about 40 to about 60 wt %, of styrenic polymer upon termination of the styrene feed.
  • the number average molecular weight of the anionic styrenic polymer product made in accordance with this particularly preferred process for preparing anionic styrenic polymers can vary, but will preferably be in the range of Mn 1000 to about Mn 10,000.
  • the anionic styrenic polymer product produced in accordance with this particularly preferred process typically will have a polydispersity which is about 1.5 or less, and preferably is about 1.2 or less.
  • a suitable process for bromination of a styrenic monomer comprises feeding a mixture of bromine and a solution of bromochloromethane and polystyrene (2.5 to 5 moles of bromine per mole of polymerized styrene in the polystyrene) to a reactor containing a further amount of bromochloromethane and a catalytic amount of AlCl 3 .
  • the mixture of polystyrene, bromochloromethane and bromine is substantially free of a bromination catalyst.
  • the phrase, “substantially free of a bromination catalyst”, is to be taken to mean less than a catalytically effective amount of catalyst.
  • reaction temperature will be within the range of from about ⁇ 10° C. to about 15° C.
  • the reaction is conducted at one or more temperatures in the range of about ⁇ 10° C. to about 10° C. as this provides product of the highest quality and, surprisingly, the reaction itself proceeds at a suitably rapid rate at these low temperatures such that the process meets commercial production requirements.
  • reaction mass is formed, it is usually maintained at reaction temperature for a period in the range of about 5 minutes to 2 hours, and preferably in the range of about 5 minutes to about 60 minutes.
  • reaction product is worked up by adding water and then settling to remove the acidic phase. Multiple water washes can be performed as desired.
  • reaction mass is treated with a base such as sodium hydroxide, sodium sulfite, and/or sodium borohydride, usually as an aqueous solution, to adjust the reaction pH to a suitable level of basicity and kill any remaining brominating agent.
  • a base such as sodium hydroxide, sodium sulfite, and/or sodium borohydride, usually as an aqueous solution
  • the reaction mass is settled to obtain a two-phase reaction mass containing an organic phase, which contains, as a solute, the brominated styrenic polymer product and an aqueous phase.
  • the aqueous phase is decanted and the remaining organic phase is stripped of its solvent component.
  • the brominated styrenic polymer product forms a precipitate.
  • the precipitate can be recovered by any liquid-solid separation technique, e.g., filtration, centrifugation, etc. The recovered precipitate is then dried. If desired, especially in the case of free-radical polystyrenes, a thermal stabilizing amount of base can be incorporated in the finished brominated anionic polystyrene composition.
  • the catalyst used in the preferred process can be any of the aluminum based catalysts, e.g., AlCl 3 , AlBr 3 and Al. Mixtures of aluminum catalysts can also be used. Once the catalyst has been added to the reaction system, it may undergo some reaction without significant loss of catalytic activity, e.g., AlCl 3 may convert to some extent to AlBr 3 . AlCl 3 , because of its availability and price, is the catalyst of choice, and powder grade AlCl 3 is most preferred due to its ease of dispersibility.
  • AlCl 3 because of its availability and price, is the catalyst of choice, and powder grade AlCl 3 is most preferred due to its ease of dispersibility.
  • the catalyst is used in an amount which is sufficient to obtain the catalytic effect sought. These catalytic amounts will depend on the activity of the catalyst, but will generally fall within the range of from about 0.2 to about 10 weight percent and preferably within the range of from about 0.5 to about 5 weight percent, based on the weight of the styrenic polymer being brominated. The most active catalysts will be used in the lower amounts, while the less active catalysts will be used in the higher amounts. When AlCl 3 is the catalyst, amounts within the range of from about 0.5 to about 3 weight percent are preferred.
  • the brominating agent is preferably bromine.
  • Bromine can be obtained commercially in the diatomic form or can be generated by the oxidation of HBr.
  • Br 2 can be supplied either as a liquid or a gas.
  • the amount of brominating agent used in the process should provide an overall mole ratio of total brominating agent to total styrenic polymer fed which will provide from about 1 to about 3 bromine substitutions per styrenic monomer unit in the polymer. It is preferred that the brominated anionic polystyrene contain at least about 60 wt % bromine, more preferably at least about 67 wt % bromine, and most preferably at least about 68 wt % bromine.
  • the amount of brominating agent used in the process will be determined by the bromine content desired considering the highest bromine content which is obtainable with the process parameters chosen. It is pointed out that as perbromination is approached, it becomes more difficult to substitute the last bromines. Adding ever larger amounts of a brominating agent does not always attenuate this difficulty. The stoichiometry is easily determined, as it requires one mole of Br 2 per substitution sought. In practice, the practitioner will determine the bromine content sought on a weight basis and then will calculate, on an idealized basis, the number of moles of brominating agent needed to obtain the same.
  • the styrenic polymer is polystyrene and the bromine content sought is 68 wt %, at least 2.7 moles of bromine per styrenic monomer unit will be required, not including any desired stoichiometric excess.
  • the mixture which is to be fed is formed from about 1 to about 8 moles of brominating agent per mole of styrenic monomer units at any time during the feed period.
  • the quantitative relationship can be constant or can vary within the above-mentioned range. (It is possible to allow for some excursions outside of the range so long as such does not do significant harm to the process efficiency or to product quality.)
  • a preferred range is from about 2.5 to about 5 moles of brominating agent per mole of styrenic monomer units to form the feed mixture.
  • the use of an amount of brominating agent in the feed mixture which gives a mole ratio of brominating agent to styrenic monomer units which is less than or greater than the selected overall mole ratio of brominating agent to styrenic monomer units will result in exhaustion of either the brominating agent or the styrenic polymer as a mixture constituent before exhaustion of the other constituent.
  • the overall molar ratio and the feed mixture ratio at least somewhat similar.
  • the initial feed should preferably contain at least a molar ratio of bromine to styrenic monomer units of 1:1.
  • the bromine used in the process be essentially anhydrous, i.e., contain less than 100 ppm (weight basis) water and contain no more than 10 ppm organic impurities, e.g., oil, grease, carbonyl containing hydrocarbons, iron, and the like.
  • the preferred organic solvent for the bromination namely, bromochloromethane
  • the bromination temperature is maintained within the range of from about ⁇ 10° C. to about 15° C. Most preferred temperatures are in the range of from about ⁇ 10° C. to about 0° C.
  • the pressure can be atmospheric, subatmospheric or superatmospheric.
  • HBr bromination of styrenic polymer will yield HBr as a major by-product.
  • the HBr formed in the process first saturates the solvent and from then on HBr escapes into the head space above the reactor contents. It is preferred that the HBr be removed and passed to a water scrubber or stored as dry HBr.
  • a dry, inert gas, e.g., nitrogen, can be used as a pad over the reactor contents to minimize the presence of water therein.
  • the polybrominated anionic styrenic polymer is a brominated styrenic polymer having (i) a bromine content of at least about 50 wt % (preferably at least about 60 wt %, and more preferably at least about 67 wt %), and (ii) thermal stability in the Thermal Stability Test described hereinafter of 200 ppm HBr or less, preferably 150 ppm of HBr or less, and more preferably 100 ppm of HBr or less.
  • Such polybrominated anionic styrenic polymer is especially suitable for use as a flame retardant when blended in at least a flame retardant amount with a thermoplastic polymer.
  • a brominated styrenic polymer which is further characterized in that it has, prior to blending, a chlorine content, if any, of less than about 700 ppm Cl, more preferably, less than about 500 ppm Cl, and still more preferably less than about 100 ppm Cl.
  • the polybrominated anionic styrenic polymer is a brominated styrenic polymer having (i) a bromine content of at least about 50 wt % (preferably at least about 60 wt %, and more preferably at least about 67 wt %), (ii) a TGA temperature for 1% weight loss which is 340° C. or higher, preferably within the range of from about 340° C. to about 380° C., and more preferably within the range of from about 345° C.
  • Such polybrominated anionic styrenic polymer is especially suitable for use as a flame retardant when blended in at least a flame retardant amount with a thermoplastic polymer.
  • Particularly preferred in this embodiment is a brominated styrenic polymer which is further characterized in that it has a chlorine content, if any, of less than about 700 ppm Cl, more preferably, less than about 500, and still more preferably less than about 100 ppm Cl.
  • the flame retardant is a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; (ii) a thermal stability in the Thermal Stability Test of 200 ppm of HBr or less, preferably 150 ppm of HBr or less, and more preferably 100 ppm of HBr or less; and (iii) a ⁇ E color value, measured using 10 wt % solutions in chlorobenzene, of less than about 10, preferably less than about 7, and more preferably less than about 5.
  • a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least
  • brominated anionic styrenic polymers of this embodiment such as brominated anionic polystyrenes have GPC weight average molecular weights in the range of about 5000 to about 30,000, preferably in the range of about 7000 to about 25,000, and more preferably in the range of about 8000 to about 20,000.
  • the polybrominated anionic styrenic polymer is a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; (ii) a thermal stability in the Thermal Stability Test of 200 ppm HBr or less, preferably 150 ppm of HBr or less, and more preferably 100 ppm HBr or less; and (iii) a melt flow index of at least about 20 g/10 min, preferably at least about 25 g/10 min, and more preferably at least about 30 g/10 min in the Melt Flow Index Test as described hereinafter.
  • brominated anionic styrenic polymers of this embodiment such as brominated anionic polystyrenes have a GPC weight average molecular weight in the range of about 5000 to about 30,000, preferably in the range of about 7000 to about 25,000, and more preferably in the range of about 8000 to about 20,000.
  • the polybrominated anionic styrenic polymer is a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; and (ii) a melt flow index of at least about 20 g/10 min, preferably at least about 25 g/10 min, and more preferably at least about 30 g/10 min in the Melt Flow Index Test as described hereinafter.
  • these brominated styrenic polymers such as brominated anionic polystyrene also have (I) a ⁇ E color value, measured using 10 wt % solutions in chlorobenzene, of less than about 10, preferably less than about 7, and more preferably less than about 5; or (II) a TGA temperature for a 1% weight loss under nitrogen of at least about 340° C., and preferably at least about 350° C.; or (III) a GPC weight average molecular weight in the range of about 5000 to about 30,000, preferably in the range of about 7000 to about 25,000, and more preferably in the range of about 8000 to about 20,000.
  • compositions of this embodiment possess at least any two of (I), (II), and (III), e.g., (I) and (II); (I) and (III); or (II) and (III). Even more preferred are compositions of this embodiment that possess all three of (I), (II), and (III).
  • a further preferred embodiment of this invention has as the flame retardant a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; (ii) a ⁇ E color value, measured using 10 wt % solutions in chlorobenzene, of less than about 10, preferably less than about 7, and more preferably less than about 5; and (iii) a GPC weight average molecular weight in the range of about 5000 to about 30,000, preferably in the range of about 7000 to about 25,000, and more preferably in the range of about 8000 to about 20,000.
  • these brominated styrenic polymers such as brominated anionic polystyrene also have a TGA temperature for a 1% weight loss under nitrogen of at least about 340° C., and preferably at least about 350° C.
  • the polybrominated anionic styrenic polymer in still another preferred embodiment of this invention is a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; (ii) a thermal stability in the Thermal Stability Test of 200 ppm HBr or less, preferably 150 ppm of HBr or less, and more preferably 100 ppm HBr or less; (iii) a melt flow index of at least about 20 g/10 min, preferably at least about 25 g/10 min, and more preferably at least about 30 g/10 min in the Melt Flow Index Test as described hereinafter; and (iv) a ⁇ E color value, measured using 10 wt % solutions in chlorobenz
  • the brominated styrenic polymers such as brominated anionic polystyrene described in this paragraph are further characterized in that they have a GPC weight average molecular weight in the range of about 5000 to about 30,000, preferably in the range of about 7000 to about 25,000, and more preferably in the range of about 8000 to about 20,000; and/or a TGA temperature for a 1% weight loss under nitrogen of at least about 340° C., and preferably at least about 350° C.
  • a further preferred embodiment of this invention has as the polybrominated anionic styrenic polymer a brominated anionic styrenic polymer, preferably a brominated anionic polystyrene, that has (i) a bromine content of at least about 50 wt %, preferably at least about 60 wt %, more preferably at least about 67 wt %, and still more preferably at least about 68 wt %; (ii) a thermal stability in the Thermal Stability Test of 200 ppm HBr or less, preferably 150 ppm HBr or less, and more preferably 100 ppm HBr or less; and (I) that is essentially free of impurities selected from the group consisting of (a) methylene chloride, (b) ethylene dichloride, and especially (c) bromodichloroethane, (d) dibromochloroethane, (e) dibromodichloroethane, (f) tribrom
  • compositions of this embodiment possess at least any two of (I), (II), and (III), e.g., (I) and (II); (I) and (III); or (II) and (III). Still more preferred are polybrominated anionic styrenic polymers that possess all three of (I), (II), and (III).
  • Particularly preferred polybrominated anionic styrenic polymers are those anionic styrenic polymers that are prepared according to the particularly preferred process for preparing anionic styrenic polymers, as described above, and then brominated, most preferably as described in this paragraph.
  • Such anionic styrenic polymer may be brominated by placing it in admixture with a brominating agent, such admixture being substantially free of a bromination catalyst, and fed to a catalytic quantity of a brominating agent.
  • a brominating agent such admixture being substantially free of a bromination catalyst
  • Another bromination method is to place the anionic styrenic polymer in solution and in admixture with a brominating agent, such admixture being substantially free of a bromination catalyst, and fed to a reactor containing a bromination catalyst and associated liquid, wherein the solvent used in forming the polystyrene solution and the liquid associated with the catalyst contains less than 200 ppm water between the two of them and the brominating agent contains less than about 100 ppm water.
  • Still another method for bromination is to contact the anionic styrenic polymer with a brominating agent in the presence of Lewis acid catalyst and solvent quantities of bromochloromethane.
  • a brominating agent for further detailed teaching of such styrenic polymer bromination process, reference is made, for example, to U.S. Pat. No. 5,767,203.
  • Yet another way to brominate the anionic polymer calls for bromochloromethane solvent and a Lewis acid catalyst to be placed in a reaction vessel, and then a brominating agent is added to the vessel.
  • the polystyrene is not placed in the reaction vessel initially; it is instead feed in admixture with the brominating agent to the reaction vessel which was previously charged with bromochloromethane solvent and a Lewis acid catalyst.
  • the polystyrene bromination process reference is made, for example, to U.S. Pat. No. 5,916,978.
  • Still another process for bromination involves a first stream comprising brominating agent, a second stream comprising anionic styrenic polymer formed as taught herein, and a third stream comprising bromination catalyst, which are fed to a mixer to intimately mix such streams.
  • styrenic polymer bromination process reference is made, for example, to U.S. Pat.
  • a bromination catalyst and associated liquid are provided in a reactor and a portion of the bromination catalyst and associated liquid is fed to a mixer external of the reactor; a brominating agent and a solution of anionic polystyrene formed in accordance with the process taught herein are fed as separate streams to the external mixer, in which the separate streams, prior to being fed to the external mixer, are substantially free of a bromination catalyst, the solvent used in forming the polystyrene solution and the liquid associated with the catalyst contains less than 200 ppm water between the two of them, and the brominating agent contains less than about 100 ppm water.
  • Bromination may also be accomplished by mixing the anionic styrenic polymer with a brominating agent and fed to a reaction vessel to which was previously added bromochloromethane solvent and a Lewis acid catalyst, the mole ratio of brominating agent to polystyrene in the feed mixture being from about 1:1 to about 8:1.
  • brominating agent to polystyrene in the feed mixture
  • bromine Content Since brominated styrenic polymers have good, or at least satisfactory, solubility in solvents such as tetrahydrofuran (THF), the determination of the bromine content for the brominated styrenic polymers is easily accomplished by using conventional X-ray fluorescence (XRF) techniques.
  • the sample analyzed is a dilute sample, say 0.1 ⁇ 0.05 g brominated anionic polystyrene in 60 mL THF.
  • the XRF spectrometer can be a Phillips PW1480 Spectrometer.
  • a standardized solution of bromobenzene in THF is used as the calibration standard.
  • the bromine values described herein are all based on the XRF analytical method.
  • ⁇ E Color Value To determine the color attributes of the brominated styrenic polymers used in this invention, use is again made of the ability to dissolve brominated styrenic polymers in easy-to-obtain solvents, such as chlorobenzene. Weigh 5 g ⁇ 0.1 g of the brominated anionic polystyrene into a 50 mL centrifuge tube. To the tube also add 45 g ⁇ 0.1 g chlorobenzene. Close the tube and shake for 1 hour on a wrist action shaker. After the 1 hour shaking period, examine the solution for undissolved solids. If a haze is present, centrifuge the solution for 10 minutes at 4000 rpm.
  • solvents such as chlorobenzene
  • the Thermal Stability Test To determine thermal stability and estimate the corrosive potential of a sample, the Thermal Stability Test is used. The test procedure, described in U.S. Pat. No. 5,637,650, is used in the following manner. Each sample is run in duplicate. A 2.00 ⁇ 0.01 g sample is placed into a new clean 20 ⁇ 150 mm test tube. With a neoprene stopper and Viton® fluoroelastomer tubing, the test tube is connected to a nitrogen purge line with exit gas from the test tube being passed successively through subsurface gas dispersion frits in three 250-mL sidearm filter flasks each containing 200 mL of 0.1 N NaOH and 5 drops of phenolphthalein.
  • test tube With a constant nitrogen purge at 0.5 SCFH, the test tube is heated at 300° C. in a molten salt bath (51.3% KNO 3 /48.7% NaNO 3 ) for 15 minutes followed by 5 minutes at ambient temperature. The test tube containing the sample is then replaced with a clean dry test tube, and the apparatus is purged with nitrogen for an additional 10 minutes with the empty test tube in the 300° C. salt bath. The test tube, tubing and gas dispersion tubes are all rinsed with deionized water, and the rinse is combined quantitatively with the solutions in the three collection flasks.
  • molten salt bath 51.3% KNO 3 /48.7% NaNO 3
  • ppm HBr ( EP 1)( N )(80912)/(sample wt. )
  • ppm HCl ( EP 2 ⁇ EP 1)( N )(36461)/(sample wt. )
  • ppm HBr equivalents ( EP 2)( N )(80912)/(sample wt.
  • the M w values were obtained by GPC using a Waters model 510 HPLC pump and, as detectors, a Waters Refractive Index Detector, Model 410 and a Precision Detector Light Scattering Detector, Model PD2000.
  • the columns were Waters, ⁇ Styragel, 500 ⁇ , 10,000 ⁇ and 100,000 ⁇ .
  • the autosampler was a Shimadzu, Model Sil 9A.
  • the solvent used was tetrahydrofuran, HPLC grade.
  • the test procedure used entailed dissolving 0.015-0.020 g of sample in 10 mL of THF. An aliquot of this solution is filtered and 50 ⁇ L is injected on the columns. The separation was analyzed using software provided by Precision Detectors for the PD 2000 Light Scattering Detector.
  • Preferred fiber compositions of this invention contain at least one flame retardant synergist.
  • Such synergists are typically used in amounts such that the weight ratio of flame retardant(s) to synergist is in the range of about 1 to about 5, and preferably in the range of about 2 to about 4.
  • flame retardant synergists include, but are not limited to, antimony trioxide, antimony pentoxide, sodium antimonate, potassium antimonate, iron oxide, and zinc borate.
  • additives are often added to the flame retardant fiber composition to impart desired properties to the end product.
  • One or more such additives may be made part of the flame retardant fiber composition of the invention.
  • the additive(s) should be chosen so that the flame retardancy and other desirable properties of the composition are not adversely affected.
  • examples of such additives include coloring agents such as dyes and pigments, stabilizers, including heat stabilizers and light stabilizers, ultraviolet absorbers, fluorescent agents, antifogging agents, weather-proofing agents, antistatic agents, fillers, lubricants, antioxidants, dispersants, blowing agents, a release agent, processing aids, nucleating agents, reinforcing agents, plasticizers, and additional polymeric materials such as elastomers or rubbers.
  • thermoplastic fiber-forming polymers or mixtures thereof.
  • antimony trioxide a synergist
  • polyethylene terephthalate is generally not compatible with polyethylene terephthalate.
  • compositions of this invention also may optionally contain a polytetrafluoroethylene resin.
  • the polytetrafluoroethylene (PTFE) resin that may be used can be prepared by any known process technique, such as emulsion or suspension polymerization, and are readily available from a number of commercial sources.
  • the polytetrafluoroethylene resin may be selected from among those resins having various degrees of polymerization (viscosity) depending upon the desired dispersibility characteristics of the PTFE resin, its processability as well as other physical properties which may be needed.
  • the carrier blend is formed from ingredients comprising (i) at least one polybrominated anionic styrenic polymer, wherein the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %, and (ii) at least one synergist or at least one other flame retardant.
  • Component (ii) may include both another flame retardant and a synergist.
  • the carrier blends may also optionally contain conventional additives, including, but not limited to, coloring agents, stabilizers, ultraviolet absorbers, antioxidants, and additional polymeric materials such as elastomers or rubbers.
  • such additive(s) should be chosen so that the flame retardancy and other desirable properties of the composition are not adversely affected.
  • the advantage of such carrier blends is that high-melting components may become part of the flame-retarded fiber composition, while minimizing the negative effects that high-melting components usually have on fiber properties.
  • the polybrominated anionic styrenic polymer is as described above for the compositions of the invention; preferred polybrominated anionic styrenic polymers are also as described above.
  • the synergist and/or flame retardant has a melting or softening point above the compounding temperature of the blend (i.e., it is high-melting or non-melting)
  • the polybrominated anionic styrenic polymer generally comprises at least about 40 weight % of the carrier blend. More preferably, the polybrominated anionic styrenic polymer comprises at least about 50 weight % of the carrier blend.
  • the synergists are as described above for the compositions of the invention.
  • any synergist or flame retardant that is high-melting can be blended with the polybrominated anionic styrenic polymer to form a carrier blend.
  • the synergist and/or flame retardant has a melting or softening point below the compounding temperature of the blend
  • the polybrominated anionic styrenic polymer can comprise less than 40 weight % of the carrier blend.
  • Preferred carrier blends include those comprised of brominated anionic polystyrene and antimony trioxide; brominated anionic polystyrene and antimony pentoxide; brominated anionic polystyrene and sodium antimonate; and brominated anionic polystyrene and ethylenebis(tetrabromophthalimide); these blends are more preferred when the brominated anionic polystyrene has a typical bromine content of approximately 60 wt % formed from anionic polystyrene.
  • Especially preferred carrier blends are those in which the brominated anionic polystyrene has a typical bromine content of approximately 68 wt % formed from anionic polystyrene.
  • Carrier blends may be formed by mixing and melting together the polybrominated anionic styrenic polymer and the synergist and/or other flame retardant, and other optional ingredients, if any.
  • the polybrominated anionic styrenic polymer, the synergist(s) and/or other flame retardant(s), and other ingredients, if any, may be added to the device or zone in which they are to be melted, where they are simultaneously mixed and melted (preferred), or melted together and then mixed.
  • Another method for blending the polybrominated anionic styrenic polymer and synergist and/or other flame retardant is to melt one of them, normally the polybrominated anionic styrenic polymer, and then add the other of them, usually while mixing and melting.
  • the polybrominated anionic styrenic polymer, the synergist and/or other flame retardant, and other optional ingredients may be (pre)mixed and then melted together. Premixing of the dry ingredients is not usually necessary, and is not preferred. If the polybrominated anionic styrenic polymer, the synergist and/or other flame retardant, and, if desired, other ingredients are premixed prior to the melting, such premixing can be done in a mixing machine, such as, for example, a Henschel mixer, a tumble mixer, and the like. A part or the entirety of any or all of the components may be pulverized in order to facilitate their dispersion in the mixture, although this is generally not necessary.
  • the compounding of the blend of the polybrominated anionic styrenic polymer and the synergist and/or other flame retardant, and other optional ingredients, if any, can be done on compounding equipment such as e.g., a twin screw extruder or a Buss kneader.
  • the polybrominated anionic styrenic polymer, synergist and/or other flame retardant, and optional other ingredients are melted and mixed together without premixing, they are usually heated until the polybrominated anionic styrenic polymer softens or melts, and then all of the components are thoroughly mixed, after which the mixture is extruded.
  • the melting and mixing can be conducted using such equipment as a single or multiple screw extruder, e.g, a twin-screw extruder, a Buss kneader, and the like.
  • the extruded strands exiting the extruder die are die-face pelletized while the mixture is cooled.
  • Water cooling or air cooling may be employed.
  • the temperature of the water is preferably at least about 60° C.; more preferably, the water temperature is in the range of about 60-70° C. More preferably, a spray of water is used.
  • air cooling by blowing a stream of air upon the extruding carrier blend), particularly when the synergist and/or other flame retardant is high-melting.
  • the lower viscosity and greater thermal stability of the polybrominated anionic styrenic polymer are believed to increase the ease of forming flame-retardant fibers and filaments.
  • One method for forming such fibers or filaments is a process which comprises melt spinning (a) at least one fiber-forming thermoplastic polymer, and (b) at least one polybrominated anionic styrenic polymer.
  • the polybrominated anionic styrenic polymer has a bromine content of at least about 50 wt %.
  • the polybrominated anionic styrenic polymer, the fiber-forming thermoplastic polymer, and other ingredients, if any, may be added to the device or zone in which they are to be melted and spun, where they are simultaneously mixed and melted (preferred), or melted together, then mixed, and then extruded.
  • the flame retardant and the fiber-forming polymer may be blended by melting one component, normally the fiber-forming polymer, and then adding the other component, usually while mixing and melting.
  • the polybrominated anionic styrenic polymer, the fiber-forming thermoplastic polymer, and other optional ingredients may be (pre)mixed, then melted together, and then extruded. Premixing of the dry ingredients is not usually necessary, and is not preferred.
  • the polybrominated anionic styrenic polymer, the fiber-forming thermoplastic polymer, and, if desired, other ingredients are premixed prior to the melting, such premixing can be done in a mixing machine, such as, for example, a Henschel mixer, a tumble mixer, and the like. A part or the entirety of any or all of the components may be pulverized in order to facilitate their dispersion in the mixture, although this is generally not necessary.
  • the polybrominated anionic styrenic polymer, the fiber-forming thermoplastic polymer, and optional other ingredients are subjected to melt spinning without premixing, they are usually heated until the polybrominated anionic styrenic polymer and the fiber-forming thermoplastic polymer soften or melt, and then all of the components are thoroughly mixed, after which the mixture is extruded.
  • the melting and mixing can be conducted using such equipment as a Banbury mixer, an open roller, a kneader, a single or multiple screw extruder, and the like.
  • Typical proportions in a masterbatch are 90:10 polybrominated anionic styrenic polymer:thermoplastic fiber-forming polymer; other typical ratios are 80:20 and 70:30 polybrominated anionic styrenic polymer:thermoplastic fiber-forming polymer (all ratios are by weight).
  • the ratio of the polybrominated anionic styrenic polymer to the thermoplastic fiber-forming polymer can be anywhere from 99:1 to 1:99.
  • the proportions can be, e.g., 30:60:10 polybrominated anionic styrenic polymer:thermoplastic fiber-forming polymer:synergist (all ratios are by weight); this ratio can be varied very widely, and is not limited by the presence of the synergist.
  • the masterbatch is later re-melted with more of the thermoplastic fiber-forming polymer to form an end product with the desired ratios of flame retardant and thermoplastic fiber-forming polymer.
  • This approach can be used in the present invention with any of the above-described mixing methods.
  • Other desired ingredients if any, may be added to the concentrated blend or added when the concentrated blend is mixed with more of the thermoplastic fiber-forming polymer.
  • the extruded strands exiting the extruder die are die-face pelletized while the mixture is cooled. Hot or cold water cooling or air cooling may be used.
  • the fiber-forming thermoplastic polymer is subjected to melt spinning with a carrier blend of this invention.
  • Optional ingredients can be added at this point, if desired, rather than as part of the carrier blend.
  • the methods for forming fibers and filaments from carrier blends are similar to those already described for the process for melt spinning a polybrominated anionic styrenic polymer and a thermoplastic fiber-forming polymer.
  • fibers and filaments can be produced in a variety of linear densities.
  • fibers and filaments with a linear density of about 2 to about 25 denier (about 0.22 to about 2.77 tex) are used for nonwoven, woven, and knitted fabrics. Fibers and filaments with such linear densities can be achieved by this invention.
  • the homogeneity of the blends of polybrominated anionic styrenic polymers with thermoplastic fiber-forming polymers allows microfiber-sized fibers and filaments (about 1 denier or less) to be produced.
  • fibers and filaments with linear densities of about 25 denier or greater can also be produced, if the application calls for such a value.
  • Preferred fibers and filaments of this invention have a linear density in the range of about 2 to about 25 denier; more preferred are fibers and filaments having a linear density in the range of about 2 to about 25 denier in which the polybrominated anionic styrenic polymer is a brominated anionic polystyrene.
  • Highly preferred fibers and filaments are those in which the linear density in the range of about 2 to about 25 denier, and the polybrominated anionic styrenic polymer is a brominated anionic polystyrene having a bromine content of at least about 60 wt %; even more highly preferred is such a filament or fiber in which the bromine content is at least about 68 wt %.
  • melt spinning is a uniaxial extension process, and the elongational viscosity behavior, which is the stress-strain relationship in uniaxial extension, is more important than the shear viscosity behavior.
  • narrower molecular weight distributions tend to be less thinning, and elongational viscosity increases at higher extension rates. This leads to higher melt orientation, which in turn is reflected in higher spun fiber or filament orientation, higher tenacity, and lower extensibility.
  • broad molecular weight distributions tend to be more thinning and hence more prone to necking and fracture at high spinning speeds.
  • the narrow molecular weight distribution of the polybrominated anionic styrenic polymer impart significant advantages to the processing of flame-retarded fibers and filaments of the invention when undergoing melt spinning.
  • the fibers and filaments of this invention once formed, can be formed into threads or yarns for producing fabrics that are woven or knitted in conventional textile processes.
  • the fibers and filaments formed by the extrusion process can also be used to form nonwoven fabrics.
  • the fibers or filaments may be used as components of blends with other fibers, such as polyester/cotton blends, that are in turn formed into nonwoven, woven, or knitted fabrics.
  • Fabrics or textiles made from the fibers and filaments of this invention can be used in carpeting (especially in high-pile carpeting), curtains, draperies, blinds, upholstery (e.g., furniture, airplane seats), tablecloths, bedding, wallcoverings, and the like.
  • a melt spinning apparatus dried polyethylene terephthalate is mixed with the desired amount of polybrominated anionic styrenic polymer at 280′-300° C., and the melt is extruded into a water bath as strands.
  • the fibers obtained are woven to form a fabric.
  • the fabric is subjected to the small-scale NFPA-701 test (1989), a standard test established by the National Fire Protection Association.
  • NFPA-701 test a 2 inch by 10 inch piece of cloth is stretched taut over a frame, and hung vertically. This piece of fabric is put three-fourths of an inch into a 1.5 inch flame for 12 seconds. The char length, drip burn, and weight loss of the fabric are measured.
  • a material should have a drip burn time of zero seconds.
  • the desired amount of polybrominated anionic styrenic polymer is added to a molten nylon (polyamide), and the melt is extruded to give fibers or filaments.
  • the fibers or filaments are knitted to form a fabric. Flame retardancy is evaluated by subjecting the fabric to the NFPA-701 test as described in Example 1.
  • the desired amount of polybrominated anionic styrenic polymer is added to a molten polypropylene, and the melt is extruded to give fibers or filaments.
  • the fibers or filaments are woven to form a fabric.
  • the fabric is subjected to the NFPA-701 test as described in Example 1.
  • Carrier blends of brominated anionic polystyrene with antimony trioxide (White Star N, Campine N. V., Beerse, Belgium) were made in a weight ratio of 77.5% brominated anionic polystyrene to 22.5% antimony trioxide. Two runs of this blend were performed. One run, Run 3, was water-cooled, while the other run, Run 4, was air-cooled. Other conditions, listed in Table 1, were the same for both runs.
  • Run 8 was water-cooled; Run 9 was cooled with a spray of water; Run 10 was air-cooled.
  • the granules were less glossy than those having higher relative proportions of brominated anionic polystyrene, which indicated that the material in the 40%/60% blends was less well compounded.
  • Runs 3-4 and 8-10 it was observed that although water-cooling shattered the granules, glossy granules were obtained by air-cooling instead. Presumably, granules from Runs 3, 8, and 9 will not shatter if they are air-cooled.
  • the first number is the relative amount of brominated anionic polystyrene in the carrier blend; the second number is the relative amount of the other component present in the carrier blend.
  • TABLE 1 Run 1 1 2 1 3-4 5 6 7 8-10 Proportions 100% 100% 77.5%/22.5% 50%/50% 45%/55% 40%/60%, 40%/60% warmer water cool only Screw 200 rpm 200 rpm 200 rpm 220 rpm 220 rpm 220 rpm 220 rpm 220 rpm speed Current — — 12 amps 17 amps 19 amps 21 amps 17 amps Throughput 15 kg/hr 15 kg/hr 10 kg/hr 15 kg/hr 12 kg/hr 12 kg/hr 12 kg/hr 12 kg/hr 12 kg/hr Pressure — 16 bar 29 bar 38 bar 54 bar 68 bar 71 bar Melting — 220° C.
  • Zone 9 180° C. 190° C. 195° C. 195° C. 195° C. 195° C. 210° C.
  • Zone 10 200° C. 200° C. 205° C. 205° C. 205° C. 205° C. 210° C.
  • Zone 11 200° C. 215° C. 215° C. 210° C. 210° C. 210° C. 1 Comparative runs 2 This is the melting temperature of the blended mixture.
  • Zone 1 240° C. 240° C. 240° C. 240° C. Zone 2 230° C. 230° C. 230° C. Zone 3 230° C. 230° C. 230° C. 230° C. Zone 4 200° C. 200° C. 200° C. 200° C. Zone 5 190° C. 190° C. 190° C. 190° C. Zone 6 190° C. 190° C. 180° C. 190° C. Zone 7 190° C.
  • reactants and components referred to by chemical name or formula anywhere in this document, whether referred to in the singular or plural, are identified as they exist prior to coming into contact with another substance referred to by chemical name or chemical type (e.g., another reactant, a solvent, or etc.). It matters not what preliminary chemical changes, transformations and/or reactions, if any, take place in the resulting mixture or solution or reaction medium as such changes, transformations and/or reactions are the natural result of bringing the specified reactants and/or components together under the conditions called for pursuant to this disclosure.
  • the reactants and components are identified as ingredients to be brought together in connection with performing a desired chemical operation or reaction or in forming a mixture to be used in conducting a desired operation or reaction.
  • an embodiment may refer to substances, components and/or ingredients in the present tense (“is comprised of”, “comprises”, “is”, etc.), the reference is to the substance, component or ingredient as it existed at the time just before it was first contacted, blended or mixed with one or more other substances, components and/or ingredients in accordance with the present disclosure.

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US10/762,787 US20050159552A1 (en) 2004-01-21 2004-01-21 Flame retarded fibers and filaments and process of production therefor
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JP2006551045A JP4767866B2 (ja) 2004-01-21 2004-10-12 燃焼遅延性の繊維およびフィラメント並びにその製造方法
SG201006183-6A SG165312A1 (en) 2004-01-21 2004-10-12 Flame retarded fibers and filaments and process of production therefor
RU2006129939/04A RU2006129939A (ru) 2004-01-21 2004-10-12 Обеспечение огнестойкости волокон и мононитей и способ их изготовления
BRPI0418453-0A BRPI0418453A (pt) 2004-01-21 2004-10-12 fibras e filamentos retardantes de chama e processos de produção destes
ES04821608T ES2402050T3 (es) 2004-01-21 2004-10-12 Fibras y filamentos retardantes de llama y proceso de producción de estos
KR1020067014367A KR101225265B1 (ko) 2004-01-21 2004-10-12 난연 섬유 및 필라멘트와 이의 제조 방법
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IL176956A0 (en) 2006-12-10
WO2005095685A1 (en) 2005-10-13
RU2006129939A (ru) 2008-02-27
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CA2552434A1 (en) 2005-10-13
KR20060127882A (ko) 2006-12-13

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