WO2009020946A1 - Flame retardant polytrimethylene terephthalate composition - Google Patents

Flame retardant polytrimethylene terephthalate composition Download PDF

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Publication number
WO2009020946A1
WO2009020946A1 PCT/US2008/072174 US2008072174W WO2009020946A1 WO 2009020946 A1 WO2009020946 A1 WO 2009020946A1 US 2008072174 W US2008072174 W US 2008072174W WO 2009020946 A1 WO2009020946 A1 WO 2009020946A1
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Prior art keywords
group
polytrimethylene terephthalate
formula
cation
based composition
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PCT/US2008/072174
Other languages
French (fr)
Inventor
Jing Chung Chang
Christopher P. Junk
Yuanfeng Liang
Joseph P. Mckeown
Matthew Arthur Page
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E.I. Du Pont De Nemours And Company
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Application filed by E.I. Du Pont De Nemours And Company filed Critical E.I. Du Pont De Nemours And Company
Priority to CA2695906A priority Critical patent/CA2695906C/en
Priority to EP08797162A priority patent/EP2176332B1/en
Priority to CN2008801075455A priority patent/CN101802069B/en
Priority to AT08797162T priority patent/ATE514740T1/en
Priority to JP2010520253A priority patent/JP5352588B2/en
Priority to BRPI0813592-4A priority patent/BRPI0813592A2/en
Priority to KR1020107004931A priority patent/KR101530399B1/en
Priority to MX2010001547A priority patent/MX2010001547A/en
Publication of WO2009020946A1 publication Critical patent/WO2009020946A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/0008Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
    • C08K5/0066Flame-proofing or flame-retarding additives
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/36Sulfur-, selenium-, or tellurium-containing compounds
    • C08K5/41Compounds containing sulfur bound to oxygen
    • C08K5/42Sulfonic acids; Derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/17Amines; Quaternary ammonium compounds
    • C08K5/19Quaternary ammonium compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/16Nitrogen-containing compounds
    • C08K5/34Heterocyclic compounds having nitrogen in the ring
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K5/00Use of organic ingredients
    • C08K5/49Phosphorus-containing compounds
    • C08K5/50Phosphorus bound to carbon only

Definitions

  • the present invention relates to flame retardant polytrimethylene terephthalate compositions comprising a fluorinated sulfonate salts as a flame retardant additive.
  • Polytrimethylene terephthalate is generally prepared by the polycon- densation reaction of 1 ,3-propanediol with terephthalic acid or terephthalic acid esters.
  • PTT resin when compared to polyethylene terephthalate ("PET”, made with ethylene glycol as opposed to 1 ,3-propane diol) or polybutylene terephthalate (“PBT”, made with 1 ,4-butane diol as opposed to 1 ,3-propane diol), is superior in mechanical characteristics, weatherability, heat aging resistance and hydrolysis resistance.
  • PTT, PET and PBT find use in many application areas (such as carpets, home furnishings, automotive parts and electronic parts) that require a certain level of flame retardance. It is known that PTT in and of itself may, under certain circumstances, have insufficient flame retardance, which currently limits in many of these application areas.
  • PTT compositions containing halogen-type flame retardants have been widely studied.
  • GB1473369 discloses a resin composition containing polypro- pylene terephthalate or PBT, decabromodiphenyl ether, antimony trioxide and asbestos.
  • US4131594 discloses a resin composition containing PTT and a graft copolymer halogen-type flame retardant, such as a polycarbonate oligomer of decabromobiphenyl ether or tetrabromobisphenol A, antimony oxide and glass fiber.
  • a graft copolymer halogen-type flame retardant such as a polycarbonate oligomer of decabromobiphenyl ether or tetrabromobisphenol A, antimony oxide and glass fiber.
  • halogen-free flame retardant polyester formulations Processes to make polyesters flame retardant by using halogen-free flame retardants based on P-containing and N-containing compounds are well known.
  • JP-A-06/157880 describes filled polyalkylene terephthalates containing melamine cyanurate and an aromatic phosphate.
  • JP-B-3115195 describes polyesters with N-heterocyclic compounds and a polyfunctional group compound and optionally a P-based flame retardant.
  • US4203888 teaches a polyester with organic diphosphates. However the compositions do not good exhibit good thermal stability especially on prolonged heat aging.
  • EP-A-0955338, EP-A-0955333 and J P-A-O 7/310284 propose PBT resin compositions containing melamine cyanurate, ammonium polyphosphate or melamine polyphosphate, phosphate ester and glass fiber. These compositions, however, have large warpage deformation and a poor appearance when molded, and thus cannot sufficiently satisfy the market's needs.
  • US2002/0120076A1 describes a polyester molding composition with an improved combination of flowability and mechanical properties.
  • the molding composition comprises from 80 to 99.9 parts by weight of thermoplastic polyester and from 0.1 to 20 parts by weight of a polyamine-polyamide graft copolymer where the total of the parts by weight of the polyester and of the graft copolymer is 100.
  • the polyamine- polyamide graft copolymer is prepared using the following monomers: (a) from 0.5 to 25% by weight, preferably from 1 to 20% by weight, and particularly preferably from 1.5 to 16% by weight, based on the graft copolymer, of a branched polyamine having at least 4 nitrogen atoms, preferably at least 8 nitrogen atoms, and particularly preferably at least 11 nitrogen atoms, and having a number-average molar mass M n of at least 146 g/mol, preferably of at least 500 g/mol, and particularly preferably of at least 800 g/mol, and (b) polyamide-forming monomers selected from lactams, omega- aminocarboxylic acids, and/or from equimolar combinations of diamine and dicarbox- ylic acid.
  • fluorinated sulfonate salts can be blended into PTTs to effectively improve the flame retardancy properties of such PTTs.
  • the present invention thus provides a PTT-based composition
  • a PTT-based composition comprising: (a) from about 75 to about 99.9 wt% of a resin component (based on the total composition weight) comprising at least about 70 wt% PTT (based on the weight of the resin component), and (b) from about 0.02 to about 25 wt% of an additive package (based on the total composition weight), wherein the additive package comprises from about 0.02 to about 5 wt% of a fluorinated sulfonate salt as a flame retardant additive (based on the total composition weight).
  • the PTT is of the type made by polycondensation of terephthalic acid or acid equivalent and 1 ,3-propanediol, with the 1 ,3-propane diol preferably being of the type that is obtained biochemically from a renewable source ("biologically-derived" 1 ,3- propanediol).
  • the invention also relates to a process for preparing a PTT composition with improved flame retardancy, comprising the steps of:
  • the PTT composition comprises from about 0.1 to about 1 wt%, more preferably from about 0.5 to about 1 wt% percent, of the fluorinated sulfonate salt, based on the total composition weight.
  • the terms “comprises,” “comprising,” “includes,” “including,” “has,” “having” or any other variation thereof, are intended to cover a non-exclusive inclusion.
  • a process, method, article, or apparatus that comprises a list of elements is not necessarily limited to only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
  • “or” refers to an inclusive “or” and not to an exclusive “or”.
  • condition A "or" B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not pre- sent) and B is true (or present), and both A and B are true (or present).
  • the resin component (and composition as a whole) comprises a predominant amount of a PTT.
  • PTTs suitable for use in the invention are well known in the art, and conveniently prepared by polycondensation of 1 ,3-propane diol with terephthalic acid or terephthalic acid equivalent.
  • terephthalic acid equivalent is meant compounds that perform substantially like terephthalic acids in reaction with polymeric glycols and diols, as would be generally recognized by a person of ordinary skill in the relevant art.
  • Terephthalic acid equivalents for the purpose of the present invention include, for example, esters (such as dimethyl terephthalate), and ester-forming derivatives such as acid halides (e.g., acid chlorides) and anhydrides.
  • terephthalic acid and terephthalic acid esters are preferably the dimethyl ester.
  • Methods for preparation of PTTs are discussed, for example in US6277947, US6326456, US6657044, US6353062, US6538076, US2003/0220465A1 and commonly owned U.S. Patent Application No. 1 1/638919 (filed 14 December 2006, entitled "Continuous Process for Producing Poly(trimethylene Terephthalate)").
  • the 1 ,3-propanediol for use in making the PTT is preferably obtained biochemically from a renewable source ("biologically-derived" 1 ,3-propanediol).
  • a particularly preferred source of 1 ,3-propanediol is via a fermentation process using a renewable biological source.
  • a renewable biological source biochemical routes to 1 ,3-propanediol (PDO) have been described that utilize feedstocks produced from biological and renewable resources such as corn feed stock.
  • PDO biochemical routes to 1 ,3-propanediol
  • bacterial strains able to convert glycerol into 1 ,3- propanediol are found in the species Klebsiella, Citrobacter, Clostridium, and Lactobacillus. The technique is disclosed in several publications, including previously incorpo- rated US5633362, US5686276 and US5821092.
  • US5821092 discloses, inter alia, a process for the biological production of 1 ,3-propanediol from glycerol using recombinant organisms.
  • the process incorporates E. coli bacteria, transformed with a heterologous pdu diol dehydratase gene, having specificity for 1 ,2-propanediol.
  • the transformed E. coli is grown in the presence of glycerol as a carbon source and 1 ,3- propanediol is isolated from the growth media. Since both bacteria and yeasts can convert glucose (e.g., corn sugar) or other carbohydrates to glycerol, the processes disclosed in these publications provide a rapid, inexpensive and environmentally responsible source of 1 ,3-propanediol monomer.
  • the biologically-derived 1 ,3-propanediol such as produced by the processes described and referenced above, contains carbon from the atmospheric carbon dioxide incorporated by plants, which compose the feedstock for the production of the 1 ,3- propanediol.
  • the biologically-derived 1 ,3-propanediol preferred for use in the context of the present invention contains only renewable carbon, and not fossil fuel-based or petroleum-based carbon.
  • compositions of the present invention can be characterized as more natural and having less environmental impact than similar compositions comprising petroleum based diols.
  • the biologically-derived 1 ,3-propanediol, and polytrimethylene terephthalate based thereon may be distinguished from similar compounds produced from a petrochemical source or from fossil fuel carbon by dual carbon-isotopic finger printing.
  • This method usefully distinguishes chemically-identical materials, and apportions carbon material by source (and possibly year) of growth of the biospheric (plant) component.
  • the isotopes, 14 C and 13 C bring complementary information to this problem.
  • the radiocarbon dating isotope ( 14 C) with its nuclear half life of 5730 years, clearly allows one to apportion specimen carbon between fossil (“dead”) and biospheric ("alive”) feedstocks (Currie, L. A.
  • the fundamental definition relates to 0.95 times the 14 C/ 12 C isotope ratio HOxI (referenced to AD 1950). This is roughly equivalent to decay-corrected pre-lndustrial Revolution wood.
  • f M 1.1.
  • the stable carbon isotope ratio ( 13 C/ 12 C) provides a complementary route to source discrimination and apportionment.
  • the 13 C/ 12 C ratio in a given biosourced material is a consequence of the 13 C/ 12 C ratio in atmospheric carbon dioxide at the time the carbon dioxide is fixed and also reflects the precise metabolic pathway. Regional variations also occur.
  • C 3 plants such as hardwoods and conifers, are dominant in the temperate climate zones.
  • the primary CO 2 fixation or carboxylation reaction involves the enzyme ribulose-1 ,5-diphosphate carboxylase and the first stable product is a 3-carbon compound.
  • C 4 plants include such plants as tropical grasses, corn and sugar cane.
  • an additional carboxylation reaction involving another enzyme, phosphenol-pyruvate carboxylase is the primary carboxylation reaction.
  • the first stable carbon compound is a 4-carbon acid, which is subsequently decarboxylated. The CO 2 thus released is refixed by the C 3 cycle.
  • Biologically-derived 1 ,3-propanediol, and compositions comprising biologically- derived 1 ,3-propanediol may be completely distinguished from their petrochemical derived counterparts on the basis of 14 C (fivi) and dual carbon-isotopic fingerprinting, indicating new compositions of matter.
  • the ability to distinguish these prod- ucts is beneficial in tracking these materials in commerce.
  • products comprising both "new" and "old” carbon isotope profiles may be distinguished from products made only of "old” materials.
  • the instant materials may be followed in commerce on the basis of their unique profile and for the purposes of defining competition, for determining shelf life, and especially for assessing environmental impact.
  • the 1 ,3-propanediol used as a reactant or as a component of the re- actant in making PTT will have a purity of greater than about 99%, and more preferably greater than about 99.9%, by weight as determined by gas chromatographic analysis.
  • Particularly preferred are the purified 1 ,3-propanediols as disclosed in US7038092, US7098368, US708431 1 and US20050069997A1.
  • the purified 1 ,3-propanediol preferably has the following characteristics:
  • composition having a CIELAB "b * " color value of less than about 0.15 ASTM D6290
  • absorbance at 270 nm of less than about 0.075 ASTM D6290
  • PTTs useful in this invention can be PTT homopolymers (derived substantially from 1 ,3-propane diol and terephthalic acid and/or equivalent) and copolymers, by themselves or in blends. PTTs used in the invention preferably contain about 70 mole % or more of repeat units derived from 1 ,3-propane diol and terephthalic acid (and/or an equivalent thereof, such as dimethyl terephthalate).
  • the PTT may contain up to 30 mole % of repeat units made from other diols or diacids.
  • the other diacids include, for example, isophthalic acid, 1 ,4-cyclohexane di- carboxylic acid, 2,6-naphthalene dicarboxylic acid, 1 ,3-cyclohexane dicarboxylic acid, succinic acid, glutaric acid, adipic acid, sebacic acid, 1 ,12-dodecane dioic acid, and the derivatives thereof such as the dimethyl, diethyl, or dipropyl esters of these dicarboxylic acids.
  • the other diols include ethylene glycol, 1 ,4-butane diol, 1 ,2-propanediol, diethylene glycol, triethylene glycol, 1 ,3-butane diol, 1 ,5-pentane diol, 1 ,6-hexane diol, 1 ,2-, 1 ,3- and 1 ,4-cyclohexane dimethanol, and the longer chain diols and polyols made by the reaction product of diols or polyols with alkylene oxides.
  • PTT polymers useful in the present invention may also include functional monomers, for example, up to about 5 mole % of sulfonate compounds useful for imparting cationic dyeability.
  • preferred sulfonate compounds include 5-lithium sulfoisophthalate, 5-sodium sulfoisophthalate, 5-potassium sulfoi- sophthalate, 4-sodium sulfo-2,6-naphthalenedicarboxylate, tetramethylphosphonium 3,5-dicarboxybenzene sulfonate, tetrabutylphosphonium 3,5-dicarboxybenzene sulfonate, tributyl-methylphosphonium 3,5-dicarboxybenzene sulfonate, tetrabutylphosphonium 2,6-dicarboxynaphthalene-4-sulfonate, tetramethylphosphonium 2,6- dicarboxynapthalene-4-sulfonate
  • the PTTs contain at least about 80 mole %, or at least about
  • the most preferred polymer is polytrimethylene terephthalate homopolymer (polymer of substantially only 1 ,3-propane diol and terephthalic acid or equivalent).
  • the resin component may contain other polymers blended with the PTT such as PET, PBT, a nylon such nylon-6 and/or nylon-6,6, etc., and preferably contains at least about 70 wt%, or at least about 80 wt%, or at least about 90 wt%, or at least about 95 wt%, or at least about 99 wt%, PTT based on the weight of the resin component. In one preferred embodiment, PTT is used without such other polymers.
  • the PTT-based compositions of the present invention may contain additives such as antioxidants, residual catalyst, delusterants (such as TiO 2 , zinc sulfide or zinc oxide), colorants (such as dyes), stabilizers, fillers (such as calcium carbonate), antimicrobial agents, antistatic agents, optical brightners, extenders, processing aids and other functional additives, hereinafter referred to as "chip additives".
  • delusterants such as TiO 2 , zinc sulfide or zinc oxide
  • colorants such as dyes
  • stabilizers such as calcium carbonate
  • fillers such as calcium carbonate
  • antimicrobial agents such as zinc sulfide and zinc oxide
  • fillers such as calcium carbonate
  • antimicrobial agents such as zinc sulfide and zinc oxide
  • TiO 2 When used in polymer for fibers and films, TiO 2 is added in an amount of preferably at least about 0.01 wt%, more preferably at least about 0.02 wt%, and preferably up to about 5 wt%, more preferably up to about 3 wt%, and most preferably up to about 2 wt% (based on total composition weight).
  • pigment reference is made to those substances commonly referred to as pigments in the art.
  • Pigments are substances, usually in the form of a dry powder, that impart color to the polymer or article (e.g., chip or fiber).
  • Pigments can be inorganic or organic, and can be natural or synthetic.
  • pigments are inert (e.g., electroni- cally neutral and do not react with the polymer) and are insoluble or relatively insoluble in the medium to which they are added, in this case the polytrimethylene terephthalate composition. In some instances they can be soluble.
  • the flame retarding additive used in the compositions of the present invention is a fluorinated sulfonate salt.
  • the compounds are not strictly "ionic liquids", they are at times referred to as such.
  • ionic liquid refers to a liquid consisting entirely of ions. Ionic liquids are also known as liquid organic salts, fused salt, molten salts, ionic melts, nonaqueous ionic liquids, room-temperature ionic liquids, organic ionic liquids and ionic fluids. These are more fully described by A. Stark and K. R. Seddon in Vol. 26 of Kirk-Othmer Encyclopedia of Chemical Technology, 5 th edition, John Wiley & Sons, Inc., 2007, pages 836-920.
  • fluorinated refers to a compound that contains at least one fluorine in place of a hydrogen. "Fluorinated” does not by definition include “perfluori- nated", where all possible hydrogens have been replaced by fluorine.
  • the flame retardant additive is one or more fluorinated sulfonate salts of the formula (I)
  • M + is a cation selected from the group consisting of lithium, sodium, potassium, cesium, pyridinium, pyridazinium, pyrimidinium, pyrazinium, imidazolium, pyrazolium, thi- azolium, oxazolium, triazolium, phosphium and ammonium; and
  • Q ' is an anion selected from the group consisting of formula (II) and formula (III),
  • R 11 and R 12 are independently selected from the group consisting of:
  • C 1 to C 15 preferably C 1 to C 6 , straight-chain or branched fluoroalkoxy, optionally substituted with at least one member selected from the group consisting of Cl, Br, I 1 OH, NH 2 and SH;
  • the pyridinium cation preferably has the formula (IV)
  • the pyridazinium cation preferably has the formula (V)
  • the pyrimidinium cation preferably has the formula (Vl)
  • the pyrazinium cation preferably has the formula (VII)
  • the imidazolium cation preferably has the formula (VIII)
  • the pyrazolium cation preferably has the formula (IX)
  • the thiazolium cation preferably has the formula (X)
  • the oxazolium cation preferably has the formula (Xl)
  • the triazolium cation preferably has the formula (XII)
  • the phosphonium cation preferably has the formula (XIII)
  • R ⁇ and the ammonium cation preferably has the formula (XIV) R 7 R 1 Q — N + - R 8 (XiV)
  • R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are each independently selected from the group consisting of:
  • R 7 , R 8 , R 9 , and R 10 are each independently selected from the group consisting of:
  • C 3 to C 25 (preferably C 3 to C 20 ) cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N, Si, and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH 2 and SH;
  • R 1 , R 2 , R 3 , R 4 , R 5 , R 6 ' R 7 , R 8 , R 9 , and R 10 can together form a cyclic or bicyclic alkanyl or alkenyl group.
  • Sources of cations (M + ) useful for the present invention are available commercially, or may be synthesized by methods known to those skilled in the art.
  • Preferred anions Q are selected from the group consisting of fluoroalkyl sul- fonyl and bis(fluoroalkylsulfonyl)imide anions.
  • fluorinated sulfonate salts based on anions of the fomula
  • (II) include potassium 1 ,1 ,2,2-tetrafluoroethanesulfonate, potassium 1 ,1 ,2,3,3,3- hexafluoropropanesulfonate, potassium 1 , 1 ,2-trifluoro-2- (trifluoromethoxy)ethanesulfonate and potassium 1 ,1 ,2-trifluoro-2- (pentafluoroethoxy)ethanesulfonate).
  • Fluoroalkyl sulfonate salts based on anions of the formula (II) may be synthesized from perfluorinated terminal olefins or perfluorinated vinyl ethers generally according to the methods described in US2006/0276670A1 (see paragraph 14 through paragraph 65) and US2006/0276671A1 (see paragraph 12 through paragraph 88).
  • potassium sulfite and bisulfite are used as the buffer, and in another preferred embodiment the reaction is carried in the absence of a radical initiator.
  • Preferred isolation methods include freeze drying or spray drying to isolate the crude products (such as potassium 1 ,1 ,2,2- tetrafluoroethanesulfonate, potassium 1 ,1 ,2,3,3,3-hexafluoropropanesulfonate, potassium 1 ,1 ,2-trifluoro-2-(trifluoromethoxy)ethanesulfonate and potassium 1 ,1 ,2-trifluoro- 2-(pentafluoroethoxy)ethanesulfonate) from the aqueous reaction mixture, using acetone to extract the crude salts, and crystallizing such salts from the reaction mixture by cooling.
  • the crude products such as potassium 1 ,1 ,2,2- tetrafluoroethanesulfonate, potassium 1 ,1 ,2,3,3,3-hexafluoropropanesulfonate, potassium 1 ,1 ,2-trifluoro-2-(trifluoromethoxy)ethanesulf
  • fluorinated sulfonate salts based on anions of the formula
  • (III) include potassium bis(1 ,1 ,2,2-tetrafluoroethanesulfonyl)imide, potassium (1 , 1 ,2,3,3,3-hexafluoropropanesulfonyl)imide potassium (1 ,1 ,2-trifluoro-2- (trifluoromethoxy)ethanesulfonyl)imide.
  • Bis(fluoroalkylsulfonyl)imide salts based on anions of the formula (III) can be synthesized as described for the synthesis of bis(perfluoroalkylsulfonyl)imide salt compounds such as (R f SO 2 ) 2 N(-)M(+).
  • 1 ,1 ,2,2-tetrafluoroethanesulfonic acid can first be converted to the corresponding sulfonyl chloride by reaction with a suitable chlorinating reagent such as
  • PCI 5 or catechol-PCI 3 as described in US2403207 and EP-A-047946.
  • the chlorine can be replaced by fluorine using potassium fluoride in an organic solvent such as acetoni- trile to produce the sulfonyl fluoride.
  • the sulfonyl fluoride can then be recovered, and two molecules of the sulfonyl fluoride can be coupled (as described in Lyapkalo, I. M., Tetrahedron (2006) 62, 3137-3145) to make the bis(fluoroalkylsulfonyl)imide.
  • ammonium chlo- ride and triethylamine (Et 3 N) are used in an organic solvent such as acetonitrile to convert the sulfonyl fluoride to the triethylammonium (NHEt 3 ) salt of the bis(fluoroalkylsulfonyl)imide.
  • the potassium salt is then obtained by further treatment with potassium hydroxide in aqueous methanol.
  • the PTT-based compositions of the invention may be prepared by conventional blending techniques well known to those skilled in the art, e.g. compounding in a poly- mer extruder, melt blending, etc.
  • the resin component and flame retardant additive(s) are melt blended. More specifically they are mixed and heated at a temperature sufficient to form a melt blend, and spun into fibers or formed into shaped articles, preferably in a continuous manner.
  • the ingredients can be formed into a blended composition in many different ways. For instance, they can be (a) heated and mixed simultaneously, (b) pre-mixed in a separate apparatus before heating, or (c) heated and then mixed.
  • the mixing, heating and forming can be carried out by conventional equipment designed for that purpose such as extruders, Banbury mixers or the like.
  • the temperature should be above the melting points of each component but below the lowest de- composition temperature, and accordingly must be adjusted for any particular composition of PTT and flame retardant additive.
  • the temperature is typically in the range of about 180 0 C to about 270 0 C.
  • the amount of fluorinated sulfonate salt additive utilized is preferably from about 0.02 to about 5 wt%, based on total composition weight. More preferably, the PTT composition comprises from about 0.1 to about 1 wt%, and still more preferably from about 0.5 to about 1 wt% percent, of the fluorinated sulfonate salt, based on the total composition weight.
  • the PTT-based compositions of this invention is useful in fibers, fabrics, films and other useful articles, and methods of making such compositions and articles, as disclosed in a number of the previously incorporated references. They may be used, for example, for producing continuous and cut (e.g., staple) fibers, yarns, and knitted, woven and nonwoven textiles.
  • the fibers may be monocomponent fibers or multicom- ponent (e.g., bicomponent) fibers, and may have many different shapes and forms. They are useful for textiles and flooring.
  • a particularly preferred end use of the PTT-based compositions of the invention is in the making of fibers for carpets, such as disclosed in US7013628.
  • the PTT used in the examples was SORONA® "semi-bright" polymer available from E.I. du Pont de Nemours and Company (Wilmington, Delaware).
  • the fluorinated sulfonate salt utilized in the example was Potassium 1 ,1 ,2,2- tetrafluoroethanesulfonate (TFES-K) synthesized by the procedure described in US2006/0276671A1.
  • the approach to demonstrating flammability improvement was to (1 ) compound the flame retardant additive into the PTT, (2) cast a film of the modified PTT, and (3) test the flammability of the film to determine the flammability improvement with the flame retardant additive.
  • SORONA® polymer was dried in a vacuum oven at 120 0 C for 16 hours, and flame retardant additive was also dried in a vacuum oven at 80 0 C for 16 hours.
  • Dry polymer was fed at a rate of 18 pounds/hour to the throat of a W & P 3OA twin screw extruder (MJM #4, 30 mm screw) with a temperature profile of 190 0 C at the first zone to 250°C at the screw tip and at the one hole strand die (4.76 mm diameter).
  • Dry flame retardant additive was fed to the throat of the extruder at a rate needed to achieve the specified concentration in the polymer, for example, at a rate of 2 pounds/hour to get a 10% loading into polymer.
  • the throat of the extruder was purged with dry nitrogen gas during operation to minimize polymer degradation.
  • the extrusion system was purged with dry polymer for >3 minutes prior to introduction of each flame retardant additive. Unmodified polymer or compounded polymer strand from the 4.76 mm die was cut into pellets for further processing into film.
  • Unmodified SORONA® polymer and compounded SORONA® polymer samples were fed to the throat of a W & P 28D twin screw extruder (MGW #3, 28 mm screw).
  • the extruder throat was purged with dry nitrogen during operation to minimize degradation. Zone temperatures ranged from 200 0 C at the first zone to 240 0 C at the screw tip with a screw speed of 100 rpm.
  • Molten polymer was delivered to the film die, 254 mm wide x 4 mm height, to produce a 4 mm thick film, 254 mm wide and up to about 18 meters long.
  • the extruder system was purged with unmodified SORONA® polymer for at least 5 minutes prior to film preparation with each compounded test item.
  • test specimens were press cut from the 4 mm thick film using a 51 mm x 152 mm die. Five specimens were cut in the film longitudinal (extru- sion) direction and five specimens were cut in the transverse (perpendicular to extrusion) direction. Test film specimens were oven dried at 105°C for greater than 30 minutes followed by cooling in a desiccator for greater than 15 minutes before testing.
  • a film specimen, 51 mm x 152 mm x 4 mm, obtained as described above was held at an angle of 45°.
  • a butane flame, 19 mm in length, was applied to the lower, 51- mm width, edge of the film until ignition occurred. After the flame self extinguished, the percent of the film specimen which burned or disappeared was determined and was recorded as percent consumed. The lower the percent consumed result the better the flame retardancy of the additive.
  • Sorona® PTT film with no flame-retardant additive was prepared and tested as described above. With no flame retardant the polymer film was completely consumed by flame without self extinguishing; i.e., 100% consumed.
  • the flame retardant additive improved the flame retardance of polytrimethylene terephthalate, even at low, 0.5% additive levels.

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Abstract

Improved flame retardant polytrimethylene terephthalate compositions are provided by including a fluorinated sulfonate salt as a flame retardant additive.

Description

FLAME RETARDANT PO LYTRI M ETHYLE N E TEREPHTHALATE COMPOSITION
CROSS-REFERENCE TO RELATED APPLICATIONS
This application is related to commonly owned U.S. Application Serial No. 11/834,232, filed August 6, 2007, entitled "FLAME RETARDANT POLYTRIMETHYL- ENE TEREPHTHALATE COMPOSITION" (Internal Reference CL3587); commonly owned U.S. Application Serial No. 1 1/834,248, filed August 6, 2007, entitled "FLAME RETARDANT POLYTRIMETHYLENE TEREPHTHALATE COMPOSITION" (Internal Reference CL3879); commonly owned U.S. Application Serial No. 11/834,260, filed August 6, 2007, entitled "FLAME RETARDANT POLYTRIMETHYLENE TEREPHTHALATE COMPOSITION" (Internal Reference CL3880); and commonly owned U.S. Application Serial No. 11/834,289, filed August 6, 2007, entitled "FLAME RETARDANT POLYTRIMETHYLENE TEREPHTHALATE COMPOSITION" (Internal Reference CL3942).
FIELD OF THE INVENTION
The present invention relates to flame retardant polytrimethylene terephthalate compositions comprising a fluorinated sulfonate salts as a flame retardant additive.
BACKGROUND OF THE INVENTION
Polytrimethylene terephthalate ("PTT") is generally prepared by the polycon- densation reaction of 1 ,3-propanediol with terephthalic acid or terephthalic acid esters. PTT resin, when compared to polyethylene terephthalate ("PET", made with ethylene glycol as opposed to 1 ,3-propane diol) or polybutylene terephthalate ("PBT", made with 1 ,4-butane diol as opposed to 1 ,3-propane diol), is superior in mechanical characteristics, weatherability, heat aging resistance and hydrolysis resistance.
PTT, PET and PBT find use in many application areas (such as carpets, home furnishings, automotive parts and electronic parts) that require a certain level of flame retardance. It is known that PTT in and of itself may, under certain circumstances, have insufficient flame retardance, which currently limits in many of these application areas. There have been several attempts to improve the flame retardance properties of PTT compositions through the addition of various flame retardant additives. For example, PTT compositions containing halogen-type flame retardants have been widely studied. For example, GB1473369 discloses a resin composition containing polypro- pylene terephthalate or PBT, decabromodiphenyl ether, antimony trioxide and asbestos. US4131594 discloses a resin composition containing PTT and a graft copolymer halogen-type flame retardant, such as a polycarbonate oligomer of decabromobiphenyl ether or tetrabromobisphenol A, antimony oxide and glass fiber.
Several attempts have been made to prepare halogen-free flame retardant polyester formulations. Processes to make polyesters flame retardant by using halogen-free flame retardants based on P-containing and N-containing compounds are well known. Thus JP-A-06/157880 describes filled polyalkylene terephthalates containing melamine cyanurate and an aromatic phosphate. JP-B-3115195 describes polyesters with N-heterocyclic compounds and a polyfunctional group compound and optionally a P-based flame retardant. US4203888 teaches a polyester with organic diphosphates. However the compositions do not good exhibit good thermal stability especially on prolonged heat aging.
EP-A-0955338, EP-A-0955333 and J P-A-O 7/310284 propose PBT resin compositions containing melamine cyanurate, ammonium polyphosphate or melamine polyphosphate, phosphate ester and glass fiber. These compositions, however, have large warpage deformation and a poor appearance when molded, and thus cannot sufficiently satisfy the market's needs.
US2002/0120076A1 describes a polyester molding composition with an improved combination of flowability and mechanical properties. The molding composition comprises from 80 to 99.9 parts by weight of thermoplastic polyester and from 0.1 to 20 parts by weight of a polyamine-polyamide graft copolymer where the total of the parts by weight of the polyester and of the graft copolymer is 100. The polyamine- polyamide graft copolymer is prepared using the following monomers: (a) from 0.5 to 25% by weight, preferably from 1 to 20% by weight, and particularly preferably from 1.5 to 16% by weight, based on the graft copolymer, of a branched polyamine having at least 4 nitrogen atoms, preferably at least 8 nitrogen atoms, and particularly preferably at least 11 nitrogen atoms, and having a number-average molar mass Mn of at least 146 g/mol, preferably of at least 500 g/mol, and particularly preferably of at least 800 g/mol, and (b) polyamide-forming monomers selected from lactams, omega- aminocarboxylic acids, and/or from equimolar combinations of diamine and dicarbox- ylic acid.
There still is a need to provide PTT compositions with improved flame retar- dancy properties.
SUMMARY OF THE INVENTION
In accordance with the present invention, it has been found that fluorinated sulfonate salts can be blended into PTTs to effectively improve the flame retardancy properties of such PTTs.
The present invention thus provides a PTT-based composition comprising: (a) from about 75 to about 99.9 wt% of a resin component (based on the total composition weight) comprising at least about 70 wt% PTT (based on the weight of the resin component), and (b) from about 0.02 to about 25 wt% of an additive package (based on the total composition weight), wherein the additive package comprises from about 0.02 to about 5 wt% of a fluorinated sulfonate salt as a flame retardant additive (based on the total composition weight).
The PTT is of the type made by polycondensation of terephthalic acid or acid equivalent and 1 ,3-propanediol, with the 1 ,3-propane diol preferably being of the type that is obtained biochemically from a renewable source ("biologically-derived" 1 ,3- propanediol).
The invention also relates to a process for preparing a PTT composition with improved flame retardancy, comprising the steps of:
a) providing the fluorinated sulfonate salt and the PTT;
b) mixing the PTT and the fluorinated sulfonate salt to form a mixture; and
c) heating and blending the mixture with agitation to form the composition.
Another aspect of the invention relates to articles (such as fibers, films and molded parts) comprising the PTT composition, such articles having improved flame retardant properties. Preferably the PTT composition comprises from about 0.1 to about 1 wt%, more preferably from about 0.5 to about 1 wt% percent, of the fluorinated sulfonate salt, based on the total composition weight.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
All publications, patent applications, patents and other references mentioned herein, if not otherwise indicated, are explicitly incorporated by reference herein in their entirety for all purposes as if fully set forth.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. In case of conflict, the present specification, including definitions, will control.
Except where expressly noted, trademarks are shown in upper case.
Unless stated otherwise, all percentages, parts, ratios, etc., are by weight.
When an amount, concentration, or other value or parameter is given as either a range, preferred range or a list of upper preferable values and lower preferable values, this is to be understood as specifically disclosing all ranges formed from any pair of any upper range limit or preferred value and any lower range limit or preferred value, regardless of whether ranges are separately disclosed. Where a range of numerical values is recited herein, unless otherwise stated, the range is intended to include the endpoints thereof, and all integers and fractions within the range. It is not intended that the scope of the invention be limited to the specific values recited when defining a range.
When the term "about" is used in describing a value or an end-point of a range, the disclosure should be understood to include the specific value or end-point referred to.
As used herein, the terms "comprises," "comprising," "includes," "including," "has," "having" or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a process, method, article, or apparatus that comprises a list of elements is not necessarily limited to only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus. Further, unless expressly stated to the contrary, "or" refers to an inclusive "or" and not to an exclusive "or". For example, a condition A "or" B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not pre- sent) and B is true (or present), and both A and B are true (or present).
Use of "a" or "an" are employed to describe elements and components of the invention. This is done merely for convenience and to give a general sense of the invention. This description should be read to include one or at least one and the singular also includes the plural unless it is obvious that it is meant otherwise.
The materials, methods, and examples herein are illustrative only and, except as specifically stated, are not intended to be limiting. Although methods and materials similar or equivalent to those described herein can be used in the practice or testing of the present invention, suitable methods and materials are described herein.
Resin Component
As indicated above, the resin component (and composition as a whole) comprises a predominant amount of a PTT.
PTTs suitable for use in the invention are well known in the art, and conveniently prepared by polycondensation of 1 ,3-propane diol with terephthalic acid or terephthalic acid equivalent.
By "terephthalic acid equivalent" is meant compounds that perform substantially like terephthalic acids in reaction with polymeric glycols and diols, as would be generally recognized by a person of ordinary skill in the relevant art. Terephthalic acid equivalents for the purpose of the present invention include, for example, esters (such as dimethyl terephthalate), and ester-forming derivatives such as acid halides (e.g., acid chlorides) and anhydrides.
Preferred are terephthalic acid and terephthalic acid esters, more preferably the dimethyl ester. Methods for preparation of PTTs are discussed, for example in US6277947, US6326456, US6657044, US6353062, US6538076, US2003/0220465A1 and commonly owned U.S. Patent Application No. 1 1/638919 (filed 14 December 2006, entitled "Continuous Process for Producing Poly(trimethylene Terephthalate)"). The 1 ,3-propanediol for use in making the PTT is preferably obtained biochemically from a renewable source ("biologically-derived" 1 ,3-propanediol).
A particularly preferred source of 1 ,3-propanediol is via a fermentation process using a renewable biological source. As an illustrative example of a starting material from a renewable source, biochemical routes to 1 ,3-propanediol (PDO) have been described that utilize feedstocks produced from biological and renewable resources such as corn feed stock. For example, bacterial strains able to convert glycerol into 1 ,3- propanediol are found in the species Klebsiella, Citrobacter, Clostridium, and Lactobacillus. The technique is disclosed in several publications, including previously incorpo- rated US5633362, US5686276 and US5821092. US5821092 discloses, inter alia, a process for the biological production of 1 ,3-propanediol from glycerol using recombinant organisms. The process incorporates E. coli bacteria, transformed with a heterologous pdu diol dehydratase gene, having specificity for 1 ,2-propanediol. The transformed E. coli is grown in the presence of glycerol as a carbon source and 1 ,3- propanediol is isolated from the growth media. Since both bacteria and yeasts can convert glucose (e.g., corn sugar) or other carbohydrates to glycerol, the processes disclosed in these publications provide a rapid, inexpensive and environmentally responsible source of 1 ,3-propanediol monomer.
The biologically-derived 1 ,3-propanediol, such as produced by the processes described and referenced above, contains carbon from the atmospheric carbon dioxide incorporated by plants, which compose the feedstock for the production of the 1 ,3- propanediol. In this way, the biologically-derived 1 ,3-propanediol preferred for use in the context of the present invention contains only renewable carbon, and not fossil fuel-based or petroleum-based carbon. The polytrimethylene terephthalate based thereon utilizing the biologically-derived 1 ,3-propanediol, therefore, has less impact on the environment as the 1 ,3-propanediol used does not deplete diminishing fossil fuels and, upon degradation, releases carbon back to the atmosphere for use by plants once again. Thus, the compositions of the present invention can be characterized as more natural and having less environmental impact than similar compositions comprising petroleum based diols.
The biologically-derived 1 ,3-propanediol, and polytrimethylene terephthalate based thereon, may be distinguished from similar compounds produced from a petrochemical source or from fossil fuel carbon by dual carbon-isotopic finger printing. This method usefully distinguishes chemically-identical materials, and apportions carbon material by source (and possibly year) of growth of the biospheric (plant) component. The isotopes, 14C and 13C, bring complementary information to this problem. The radiocarbon dating isotope (14C), with its nuclear half life of 5730 years, clearly allows one to apportion specimen carbon between fossil ("dead") and biospheric ("alive") feedstocks (Currie, L. A. "Source Apportionment of Atmospheric Particles," Characterization of Environmental Particles, J. Buffle and H. P. van Leeuwen, Eds., 1 of Vol. I of the IUPAC Environmental Analytical Chemistry Series (Lewis Publishers, Inc) (1992) 3-74). The basic assumption in radiocarbon dating is that the constancy of 14C con- centration in the atmosphere leads to the constancy of 14C in living organisms. When dealing with an isolated sample, the age of a sample can be deduced approximately by the relationship:
t = (-5730/0.693)ln(A/A0)
wherein t = age, 5730 years is the half-life of radiocarbon, and A and A0 are the spe- cific 14C activity of the sample and of the modern standard, respectively (Hsieh, Y., Soil Sci. Soc. Am J., 56, 460, (1992)). However, because of atmospheric nuclear testing since 1950 and the burning of fossil fuel since 1850, 14C has acquired a second, geo- chemical time characteristic. Its concentration in atmospheric CO2, and hence in the living biosphere, approximately doubled at the peak of nuclear testing, in the mid- 1960s. It has since been gradually returning to the steady-state cosmogenic (atmospheric) baseline isotope rate (14C/12C) of ca. 1.2 x 10"12, with an approximate relaxation "half-life" of 7-10 years. (This latter half-life must not be taken literally; rather, one must use the detailed atmospheric nuclear input/decay function to trace the variation of atmospheric and biospheric 14C since the onset of the nuclear age.) It is this latter bio- spheric 14C time characteristic that holds out the promise of annual dating of recent biospheric carbon. 14C can be measured by accelerator mass spectrometry (AMS), with results given in units of "fraction of modern carbon" (fM). fM is defined by National Institute of Standards and Technology (NIST) Standard Reference Materials (SRMs) 4990B and 4990C, known as oxalic acids standards HOxI and HOxII, respectively. The fundamental definition relates to 0.95 times the 14C/12C isotope ratio HOxI (referenced to AD 1950). This is roughly equivalent to decay-corrected pre-lndustrial Revolution wood. For the current living biosphere (plant material), fM =1.1. The stable carbon isotope ratio (13C/12C) provides a complementary route to source discrimination and apportionment. The 13C/12C ratio in a given biosourced material is a consequence of the 13C/12C ratio in atmospheric carbon dioxide at the time the carbon dioxide is fixed and also reflects the precise metabolic pathway. Regional variations also occur. Petroleum, C3 plants (the broadleaf), C4 plants (the grasses), and marine carbonates all show significant differences in 13C/12C and the corresponding δ 13C values. Furthermore, lipid matter of C3 and C4 plants analyze differently than materials derived from the carbohydrate components of the same plants as a consequence of the metabolic pathway. Within the precision of measurement, 13C shows large variations due to isotopic fractionation effects, the most significant of which for the instant invention is the photosynthetic mechanism. The major cause of differences in the carbon isotope ratio in plants is closely associated with differences in the pathway of photosynthetic carbon metabolism in the plants, particularly the reaction occurring during the primary carboxylation, i.e., the initial fixation of atmospheric CO2. Two large classes of vegetation are those that incorporate the "C3" (or Calvin-Benson) photosynthetic cycle and those that incorporate the "C4" (or Hatch-Slack) photosynthetic cycle. C3 plants, such as hardwoods and conifers, are dominant in the temperate climate zones. In C3 plants, the primary CO2 fixation or carboxylation reaction involves the enzyme ribulose-1 ,5-diphosphate carboxylase and the first stable product is a 3-carbon compound. C4 plants, on the other hand, include such plants as tropical grasses, corn and sugar cane. In C4 plants, an additional carboxylation reaction involving another enzyme, phosphenol-pyruvate carboxylase, is the primary carboxylation reaction. The first stable carbon compound is a 4-carbon acid, which is subsequently decarboxylated. The CO2 thus released is refixed by the C3 cycle.
Both C4 and C3 plants exhibit a range of 13C/12C isotopic ratios, but typical values are ca. -10 to -14 per mil (C4) and -21 to -26 per mil (C3) (Weber et al., J. Aqric. Food Chem., 45, 2942 (1997)). Coal and petroleum fall generally in this latter range. The 13C measurement scale was originally defined by a zero set by pee dee belemnite (PDB) limestone, where values are given in parts per thousand deviations from this material. The "513C" values are in parts per thousand (per mil), abbreviated %o, and are calculated as follows:
513C ≡ (13C/12C)sample - (13C/12C)standard x 1000%o (13C/12C)standard Since the PDB reference material (RM) has been exhausted, a series of alternative RMs have been developed in cooperation with the IAEA, USGS, NIST, and other selected international isotope laboratories. Notations for the per mil deviations from PDB is 513C. Measurements are made on CO2 by high precision stable ratio mass spec- trometry (IRMS) on molecular ions of masses 44, 45 and 46.
Biologically-derived 1 ,3-propanediol, and compositions comprising biologically- derived 1 ,3-propanediol, therefore, may be completely distinguished from their petrochemical derived counterparts on the basis of 14C (fivi) and dual carbon-isotopic fingerprinting, indicating new compositions of matter. The ability to distinguish these prod- ucts is beneficial in tracking these materials in commerce. For example, products comprising both "new" and "old" carbon isotope profiles may be distinguished from products made only of "old" materials. Hence, the instant materials may be followed in commerce on the basis of their unique profile and for the purposes of defining competition, for determining shelf life, and especially for assessing environmental impact.
Preferably the 1 ,3-propanediol used as a reactant or as a component of the re- actant in making PTT will have a purity of greater than about 99%, and more preferably greater than about 99.9%, by weight as determined by gas chromatographic analysis. Particularly preferred are the purified 1 ,3-propanediols as disclosed in US7038092, US7098368, US708431 1 and US20050069997A1.
The purified 1 ,3-propanediol preferably has the following characteristics:
(1 ) an ultraviolet absorption at 220 nm of less than about 0.200, and at 250 nm of less than about 0.075, and at 275 nm of less than about 0.075; and/or
(2) a composition having a CIELAB "b*" color value of less than about 0.15 (ASTM D6290), and an absorbance at 270 nm of less than about 0.075; and/or
(3) a peroxide composition of less than about 10 ppm; and/or
(4) a concentration of total organic impurities (organic compounds other than 1 ,3-propanediol) of less than about 400 ppm, more preferably less than about 300 ppm, and still more preferably less than about 150 ppm, as measured by gas chromatography. PTTs useful in this invention can be PTT homopolymers (derived substantially from 1 ,3-propane diol and terephthalic acid and/or equivalent) and copolymers, by themselves or in blends. PTTs used in the invention preferably contain about 70 mole % or more of repeat units derived from 1 ,3-propane diol and terephthalic acid (and/or an equivalent thereof, such as dimethyl terephthalate).
The PTT may contain up to 30 mole % of repeat units made from other diols or diacids. The other diacids include, for example, isophthalic acid, 1 ,4-cyclohexane di- carboxylic acid, 2,6-naphthalene dicarboxylic acid, 1 ,3-cyclohexane dicarboxylic acid, succinic acid, glutaric acid, adipic acid, sebacic acid, 1 ,12-dodecane dioic acid, and the derivatives thereof such as the dimethyl, diethyl, or dipropyl esters of these dicarboxylic acids. The other diols include ethylene glycol, 1 ,4-butane diol, 1 ,2-propanediol, diethylene glycol, triethylene glycol, 1 ,3-butane diol, 1 ,5-pentane diol, 1 ,6-hexane diol, 1 ,2-, 1 ,3- and 1 ,4-cyclohexane dimethanol, and the longer chain diols and polyols made by the reaction product of diols or polyols with alkylene oxides.
PTT polymers useful in the present invention may also include functional monomers, for example, up to about 5 mole % of sulfonate compounds useful for imparting cationic dyeability. Specific examples of preferred sulfonate compounds include 5-lithium sulfoisophthalate, 5-sodium sulfoisophthalate, 5-potassium sulfoi- sophthalate, 4-sodium sulfo-2,6-naphthalenedicarboxylate, tetramethylphosphonium 3,5-dicarboxybenzene sulfonate, tetrabutylphosphonium 3,5-dicarboxybenzene sulfonate, tributyl-methylphosphonium 3,5-dicarboxybenzene sulfonate, tetrabutylphosphonium 2,6-dicarboxynaphthalene-4-sulfonate, tetramethylphosphonium 2,6- dicarboxynapthalene-4-sulfonate, ammonium 3,5-dicarboxybenzene sulfonate, and ester derivatives thereof such as methyl, dimethyl, and the like.
More preferably, the PTTs contain at least about 80 mole %, or at least about
90 mole %, or at least about 95 mole %, or at least about 99 mole %, of repeat units derived from 1 ,3-propane diol and terephthalic acid (or equivalent). The most preferred polymer is polytrimethylene terephthalate homopolymer (polymer of substantially only 1 ,3-propane diol and terephthalic acid or equivalent).
The resin component may contain other polymers blended with the PTT such as PET, PBT, a nylon such nylon-6 and/or nylon-6,6, etc., and preferably contains at least about 70 wt%, or at least about 80 wt%, or at least about 90 wt%, or at least about 95 wt%, or at least about 99 wt%, PTT based on the weight of the resin component. In one preferred embodiment, PTT is used without such other polymers.
Additive Package
The PTT-based compositions of the present invention may contain additives such as antioxidants, residual catalyst, delusterants (such as TiO2, zinc sulfide or zinc oxide), colorants (such as dyes), stabilizers, fillers (such as calcium carbonate), antimicrobial agents, antistatic agents, optical brightners, extenders, processing aids and other functional additives, hereinafter referred to as "chip additives". When used, TiO2 or similar compounds (such as zinc sulfide and zinc oxide) are used as pigments or delusterants in amounts normally used in making PTT compositions, that is up to about 5 wt% or more (based on total composition weight) in making fibers and larger amounts in some other end uses. When used in polymer for fibers and films, TiO2 is added in an amount of preferably at least about 0.01 wt%, more preferably at least about 0.02 wt%, and preferably up to about 5 wt%, more preferably up to about 3 wt%, and most preferably up to about 2 wt% (based on total composition weight).
By "pigment" reference is made to those substances commonly referred to as pigments in the art. Pigments are substances, usually in the form of a dry powder, that impart color to the polymer or article (e.g., chip or fiber). Pigments can be inorganic or organic, and can be natural or synthetic. Generally, pigments are inert (e.g., electroni- cally neutral and do not react with the polymer) and are insoluble or relatively insoluble in the medium to which they are added, in this case the polytrimethylene terephthalate composition. In some instances they can be soluble.
The flame retarding additive used in the compositions of the present invention is a fluorinated sulfonate salt. Although the compounds are not strictly "ionic liquids", they are at times referred to as such.
As used herein, the term "ionic liquid" refers to a liquid consisting entirely of ions. Ionic liquids are also known as liquid organic salts, fused salt, molten salts, ionic melts, nonaqueous ionic liquids, room-temperature ionic liquids, organic ionic liquids and ionic fluids. These are more fully described by A. Stark and K. R. Seddon in Vol. 26 of Kirk-Othmer Encyclopedia of Chemical Technology, 5th edition, John Wiley & Sons, Inc., 2007, pages 836-920. As used herein, "fluorinated" refers to a compound that contains at least one fluorine in place of a hydrogen. "Fluorinated" does not by definition include "perfluori- nated", where all possible hydrogens have been replaced by fluorine.
Preferably the flame retardant additive is one or more fluorinated sulfonate salts of the formula (I)
M+Q- (I)
wherein:
M+ is a cation selected from the group consisting of lithium, sodium, potassium, cesium, pyridinium, pyridazinium, pyrimidinium, pyrazinium, imidazolium, pyrazolium, thi- azolium, oxazolium, triazolium, phosphium and ammonium; and
Q' is an anion selected from the group consisting of formula (II) and formula (III),
Figure imgf000013_0001
wherein each of R11 and R12 are independently selected from the group consisting of:
(1 ) halogen;
(2) -CH3, -C2H5 or C3 to Ci5, preferably C3 to C6, straight-chain or branched alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, I, OH, NH2 and SH;
(3) -OCH3, -OC2H5 or C3 to C15, preferably C3 to C6, straight-chain or branched alkoxy, optionally substituted with at least one member selected from the group consisting of Cl, Br, I, OH, NH2 and SH; (4) C1 to C15, preferably C1 to C6, straight-chain or branched fluoroalkyl, optionally substituted with at least one member selected from the group consisting of Cl, Br1 I1 OH, NH2 and SH;
(5) C1 to C15, preferably C1 to C6, straight-chain or branched fluoroalkoxy, optionally substituted with at least one member selected from the group consisting of Cl, Br, I1 OH, NH2 and SH;
(6) C1 to C15, preferably C1 to C6, straight-chain or branched perfluoroalkyl; and
(7) C1 to C15, preferably C1 to C6, straight-chain or branched perfluoroalkoxy.
In the above formula (I), the pyridinium cation preferably has the formula (IV)
Figure imgf000014_0001
the pyridazinium cation preferably has the formula (V)
Figure imgf000014_0002
the pyrimidinium cation preferably has the formula (Vl)
Figure imgf000015_0001
the pyrazinium cation preferably has the formula (VII)
Figure imgf000015_0002
the imidazolium cation preferably has the formula (VIII)
Figure imgf000015_0003
the pyrazolium cation preferably has the formula (IX)
Figure imgf000015_0004
the thiazolium cation preferably has the formula (X)
Figure imgf000016_0001
the oxazolium cation preferably has the formula (Xl)
Figure imgf000016_0002
the triazolium cation preferably has the formula (XII)
Figure imgf000016_0003
the phosphonium cation preferably has the formula (XIII)
R'
Figure imgf000016_0004
R^ and the ammonium cation preferably has the formula (XIV) R7 R1 Q— N +- R8 (XiV)
R9
wherein:
R1, R2, R3, R4, R5 and R6 are each independently selected from the group consisting of:
(a) H
(b) halogen
(c) -CH3, -C2H5, or a C3 to C25 (preferably C3 to C20) straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(d) C3 to C25, preferably C3 to C20, cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N, Si, and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(e) C6 to C25 unsubstituted aryl or C6 to C25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and
(f) C6 to C25 substituted aryl or C6 to C25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of:
(1 ) -CH3, -C2H5, or C3 to C25, preferably C3 to C20, straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH, (2) OH,
(3) NH2, and
(4) SH;
R7, R8, R9, and R10 are each independently selected from the group consisting of:
(g) -CH3, -C2H5, or C3 to C25 (preferably C3 to C20) straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(h) C3 to C25 (preferably C3 to C20) cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N, Si, and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(j) C6 to C25 unsubstituted aryl or C6 to C25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and
(k) C6 to C25 substituted aryl or C6 to C25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of
(1 ) -CH3, -C2H5, or C3 to C25, preferably C3 to C20, straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH,
(2) OH,
(3) NH2, and
(4) SH; and wherein optionally at least two of R1, R2, R3, R4, R5, R6' R7, R8, R9, and R10 can together form a cyclic or bicyclic alkanyl or alkenyl group.
Sources of cations (M+) useful for the present invention are available commercially, or may be synthesized by methods known to those skilled in the art.
Preferred anions Q" are selected from the group consisting of fluoroalkyl sul- fonyl and bis(fluoroalkylsulfonyl)imide anions.
Specific examples of fluorinated sulfonate salts based on anions of the fomula
(II) include potassium 1 ,1 ,2,2-tetrafluoroethanesulfonate, potassium 1 ,1 ,2,3,3,3- hexafluoropropanesulfonate, potassium 1 , 1 ,2-trifluoro-2- (trifluoromethoxy)ethanesulfonate and potassium 1 ,1 ,2-trifluoro-2- (pentafluoroethoxy)ethanesulfonate).
Fluoroalkyl sulfonate salts based on anions of the formula (II) may be synthesized from perfluorinated terminal olefins or perfluorinated vinyl ethers generally according to the methods described in US2006/0276670A1 (see paragraph 14 through paragraph 65) and US2006/0276671A1 (see paragraph 12 through paragraph 88). In one preferred embodiment of these methods, potassium sulfite and bisulfite are used as the buffer, and in another preferred embodiment the reaction is carried in the absence of a radical initiator. Preferred isolation methods include freeze drying or spray drying to isolate the crude products (such as potassium 1 ,1 ,2,2- tetrafluoroethanesulfonate, potassium 1 ,1 ,2,3,3,3-hexafluoropropanesulfonate, potassium 1 ,1 ,2-trifluoro-2-(trifluoromethoxy)ethanesulfonate and potassium 1 ,1 ,2-trifluoro- 2-(pentafluoroethoxy)ethanesulfonate) from the aqueous reaction mixture, using acetone to extract the crude salts, and crystallizing such salts from the reaction mixture by cooling.
Specific examples of fluorinated sulfonate salts based on anions of the formula
(III) include potassium bis(1 ,1 ,2,2-tetrafluoroethanesulfonyl)imide, potassium (1 , 1 ,2,3,3,3-hexafluoropropanesulfonyl)imide potassium (1 ,1 ,2-trifluoro-2- (trifluoromethoxy)ethanesulfonyl)imide. Bis(fluoroalkylsulfonyl)imide salts based on anions of the formula (III) can be synthesized as described for the synthesis of bis(perfluoroalkylsulfonyl)imide salt compounds such as (RfSO2)2N(-)M(+). See, for example, US5847616; US625211 1 ; US6399821 ; DesMarteau, D. and Hu, L.Q., Inorα. Chem. (1993), 32, 5007-5010; and Caporiccio, G. et al, J. Fluor. Chem. (2004), 125, 243-252.
For example, 1 ,1 ,2,2-tetrafluoroethanesulfonic acid can first be converted to the corresponding sulfonyl chloride by reaction with a suitable chlorinating reagent such as
PCI5 or catechol-PCI3 as described in US2403207 and EP-A-047946. The chlorine can be replaced by fluorine using potassium fluoride in an organic solvent such as acetoni- trile to produce the sulfonyl fluoride.
Figure imgf000020_0001
The sulfonyl fluoride can then be recovered, and two molecules of the sulfonyl fluoride can be coupled (as described in Lyapkalo, I. M., Tetrahedron (2006) 62, 3137-3145) to make the bis(fluoroalkylsulfonyl)imide. According to this procedure, ammonium chlo- ride and triethylamine (Et3N) are used in an organic solvent such as acetonitrile to convert the sulfonyl fluoride to the triethylammonium (NHEt3) salt of the bis(fluoroalkylsulfonyl)imide. The potassium salt is then obtained by further treatment with potassium hydroxide in aqueous methanol.
Figure imgf000020_0002
Mixtures of one or more fluorinated sulfonate salts, as well as mixtures of one or more fluorinated sulfonate salts with one or more other flame retardant additives, are suitable for use in the present invention.
The PTT-based compositions of the invention may be prepared by conventional blending techniques well known to those skilled in the art, e.g. compounding in a poly- mer extruder, melt blending, etc. Preferably the resin component and flame retardant additive(s) are melt blended. More specifically they are mixed and heated at a temperature sufficient to form a melt blend, and spun into fibers or formed into shaped articles, preferably in a continuous manner. The ingredients can be formed into a blended composition in many different ways. For instance, they can be (a) heated and mixed simultaneously, (b) pre-mixed in a separate apparatus before heating, or (c) heated and then mixed. The mixing, heating and forming can be carried out by conventional equipment designed for that purpose such as extruders, Banbury mixers or the like. The temperature should be above the melting points of each component but below the lowest de- composition temperature, and accordingly must be adjusted for any particular composition of PTT and flame retardant additive. The temperature is typically in the range of about 1800C to about 2700C.
The amount of fluorinated sulfonate salt additive utilized is preferably from about 0.02 to about 5 wt%, based on total composition weight. More preferably, the PTT composition comprises from about 0.1 to about 1 wt%, and still more preferably from about 0.5 to about 1 wt% percent, of the fluorinated sulfonate salt, based on the total composition weight.
Uses
The PTT-based compositions of this invention is useful in fibers, fabrics, films and other useful articles, and methods of making such compositions and articles, as disclosed in a number of the previously incorporated references. They may be used, for example, for producing continuous and cut (e.g., staple) fibers, yarns, and knitted, woven and nonwoven textiles. The fibers may be monocomponent fibers or multicom- ponent (e.g., bicomponent) fibers, and may have many different shapes and forms. They are useful for textiles and flooring.
A particularly preferred end use of the PTT-based compositions of the invention is in the making of fibers for carpets, such as disclosed in US7013628.
EXAMPLES
In the following examples, all parts, percentages, etc., are by weight unless oth- erwise indicated. Ingredients
The PTT used in the examples was SORONA® "semi-bright" polymer available from E.I. du Pont de Nemours and Company (Wilmington, Delaware).
The fluorinated sulfonate salt utilized in the example was Potassium 1 ,1 ,2,2- tetrafluoroethanesulfonate (TFES-K) synthesized by the procedure described in US2006/0276671A1.
The approach to demonstrating flammability improvement was to (1 ) compound the flame retardant additive into the PTT, (2) cast a film of the modified PTT, and (3) test the flammability of the film to determine the flammability improvement with the flame retardant additive.
Flame Retardant Additive Compounding
SORONA® polymer was dried in a vacuum oven at 1200C for 16 hours, and flame retardant additive was also dried in a vacuum oven at 800C for 16 hours.
Dry polymer was fed at a rate of 18 pounds/hour to the throat of a W & P 3OA twin screw extruder (MJM #4, 30 mm screw) with a temperature profile of 1900C at the first zone to 250°C at the screw tip and at the one hole strand die (4.76 mm diameter). Dry flame retardant additive was fed to the throat of the extruder at a rate needed to achieve the specified concentration in the polymer, for example, at a rate of 2 pounds/hour to get a 10% loading into polymer. The throat of the extruder was purged with dry nitrogen gas during operation to minimize polymer degradation. The extrusion system was purged with dry polymer for >3 minutes prior to introduction of each flame retardant additive. Unmodified polymer or compounded polymer strand from the 4.76 mm die was cut into pellets for further processing into film.
Film Preparation
All samples were dried at 1200C for 16 hours before use in preparing films.
Unmodified SORONA® polymer and compounded SORONA® polymer samples were fed to the throat of a W & P 28D twin screw extruder (MGW #3, 28 mm screw). The extruder throat was purged with dry nitrogen during operation to minimize degradation. Zone temperatures ranged from 2000C at the first zone to 2400C at the screw tip with a screw speed of 100 rpm. Molten polymer was delivered to the film die, 254 mm wide x 4 mm height, to produce a 4 mm thick film, 254 mm wide and up to about 18 meters long. The extruder system was purged with unmodified SORONA® polymer for at least 5 minutes prior to film preparation with each compounded test item.
Test Sample Preparation
For each test item ten test specimens were press cut from the 4 mm thick film using a 51 mm x 152 mm die. Five specimens were cut in the film longitudinal (extru- sion) direction and five specimens were cut in the transverse (perpendicular to extrusion) direction. Test film specimens were oven dried at 105°C for greater than 30 minutes followed by cooling in a desiccator for greater than 15 minutes before testing.
Film Flammability Test
A film specimen, 51 mm x 152 mm x 4 mm, obtained as described above was held at an angle of 45°. A butane flame, 19 mm in length, was applied to the lower, 51- mm width, edge of the film until ignition occurred. After the flame self extinguished, the percent of the film specimen which burned or disappeared was determined and was recorded as percent consumed. The lower the percent consumed result the better the flame retardancy of the additive.
Comparative Example A
Sorona® PTT film with no flame-retardant additive was prepared and tested as described above. With no flame retardant the polymer film was completely consumed by flame without self extinguishing; i.e., 100% consumed.
Examples 1-2
Testing results for Comparative Example A and Examples 1-2 are presented in
Table 1. As shown, the flame retardant additive improved the flame retardance of polytrimethylene terephthalate, even at low, 0.5% additive levels.
Table 1
Figure imgf000024_0001

Claims

1. A polytrimethylene terephthalate-based composition comprising: (a) from about 75 to about 99.9 wt% of a resin component (based on the total composition weight) comprising at least about 70 wt% of a polytrimethylene terephthalate (based on the weight of the resin component), and (b) from about 0.02 to about 25 wt% of an additive package (based on the total composition weight), wherein the additive package comprises from about 0.02 to about 5 wt% of a fluorinated sulfonate salt as a flame retar- dant additive (based on the total composition weight).
2. The polytrimethylene terephthalate-based composition of claim 1 , wherein the fluorinated sulfonate salts are of the formula (I)
M+Q- (I)
wherein:
M+ is a cation selected from the group consisting of lithium, sodium, potassium, cesium, pyridinium, pyridazinium, pyrimidinium, pyrazinium, imidazolium, pyrazolium, thi- azolium, oxazolium, triazolium, phosphium and ammonium; and
Q' is an anion selected from the group consisting of formula (II) and formula (III),
Figure imgf000025_0001
wherein each of R11 and R12 are independently selected from the group consisting of:
(1 ) halogen; (2) -CH3, -C2H5 or C3 to C15 straight-chain or branched alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, I1 OH, NH2 and SH;
(3) -OCH3, -OC2H5 or C3 to Ci5 straight-chain or branched alkoxy, optionally substituted with at least one member selected from the group consisting of Cl, Br, I,
OH, NH2 and SH;
(4) C1 to C15 straight-chain or branched fluoroalkyl, optionally substituted with at least one member selected from the group consisting of Cl, Br, I, OH, NH2 and SH;
(5) C1 to C15 straight-chain or branched fluoroalkoxy, optionally substituted with at least one member selected from the group consisting of Cl, Br, I, OH, NH2 and SH;
(6) C1 to C15 straight-chain or branched perfluoroalkyl; and
(7) C1 to C15 straight-chain or branched perfluoroalkoxy.
3. The polytrimethylene terephthalate-based composition of claim 2, wherein M+ is selected from the group consisting of:
(i) a pyridinium cation of the formula (IV)
Figure imgf000026_0001
(ii) a pyridazinium cation of the formula (V)
Figure imgf000027_0001
(iii) a pyrimidinium cation of the formula (Vl)
Figure imgf000027_0002
(iv) a pyrazinium cation of the formula (VII)
Figure imgf000027_0003
(v) an imidazolium cation of the formula (VIII)
Figure imgf000027_0004
(vi) a pyrazolium cation of the formula (IX)
Figure imgf000028_0001
(vii) a thiazolium cation of the formula (X)
Figure imgf000028_0002
(viii) an oxazolium cation of the formula (Xl)
Figure imgf000028_0003
(ix) a triazolium cation of the formula (XII)
Figure imgf000028_0004
(x) a phosphonium cation of the formula (XIII) R7
Figure imgf000029_0001
R9
and (xi) an ammonium cation of the formula (XIV)
R7 R1 Q— N +- R8 (XiV)
R9
wherein:
R1, R2, R3, R4, R5 and R6 are each independently selected from the group consisting of:
(a) H
(b) halogen
(c) -CH3, -C2H5, or a C3 to C25 straight-chain, branched or cyclic alkane or al- kene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(d) C3 to C25 cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N, Si, and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(e) C6 to C25 unsubstituted aryl or C6 to C25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and
(f) C6 to C25 substituted aryl or C6 to C25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of:
(I ) -CH3, -C2H5, or C3 to C25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH,
(2) OH,
(3) NH2, and
(4) SH;
R7, R8, R9, and R10 are each independently selected from the group consisting of:
(g) -CH3, -C2H5, or C3 to C25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH;
(h) C3 to C25 cyclic alkane or alkene comprising one to three heteroatoms selected from the group consisting of O, N, Si, and S, and optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH,
NH2 and SH;
(j) C6 to C25 unsubstituted aryl or C6 to C25 unsubstituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and
(k) C6 to C25 substituted aryl or C6 to C25 substituted heteroaryl having one to three heteroatoms independently selected from the group consisting of O, N, Si, and S; and wherein said substituted aryl or substituted heteroaryl has one to three substituents independently selected from the group consisting of
(I ) -CH3, -C2H5, or C3 to C25 straight-chain, branched or cyclic alkane or alkene, optionally substituted with at least one member selected from the group consisting of Cl, Br, F, I, OH, NH2 and SH,
(2) OH, (3) NH2, and
(4) SH;
and wherein optionally at least two of R1, R2, R3, R4, R5, R6' R7, R8, R9, and R10 can together form a cyclic or bicyclic alkanyl or alkenyl group.
4. The polytrimethylene terephthalate-based composition of claim 2, wherein Q- is selected from the group consisting of fluoroalkyl sulfonyl and bis(fluoroalkylsulfonyl)imide anions.
5. The polytrimethylene terephthalate-based composition of claim 3, wherein Q- is selected from the group consisting of fluoroalkyl sulfonyl and bis(fluoroalkylsulfonyl)imide anions.
6. The polytrimethylene terephthalate-based composition of claim 1 , wherein the additive package comprises from about 0.1 to about 1 wt% of a fluorinated sulfate salt (based on total composition weight).
7. The polytrimethylene terephthalate-based composition of claim 1 , wherein the additive package comprises from about 0.5 to about 1 wt% of a fluorinated sulfate salt
(based on total composition weight).
8. The polytrimethylene terephthalate-based composition of claim 1 , wherein the polytrimethylene terephthalate is of the type made by polycondensation of terephthalic acid or acid equivalent and 1 ,3-propanediol.
9. The polytrimethylene terephthalate-based composition of claim 8, wherein the 1 ,3-propane is a biologically-derived 1 ,3-propanediol.
10. The polytrimethylene terephthalate-based composition of claim 1 , wherein the polytrimethylene terephthalate is a polytrimethylene terephthalate homopolymer.
11. The polytrimethylene terephthalate-based composition of claim 1 , wherein the resin component comprises another polymer.
12. The polytrimethylene terephthalate-based composition of claim 11 , wherein the resin component comprises a polyethylene terephthalate.
13. The polytrimethylene terephthalate-based composition of claim 11 , wherein the resin component comprises a polybutylene terephthalate.
14. The polytrimethylene terephthalate-based composition of claim 11 , wherein the resin component comprises a nylon.
15. The polytrimethylene terephthalate-based composition of claim 1 , wherein the additive package comprises a TiO2.
16. A process for preparing the polytrimethylene terephthalate-based composition of claim 1 , comprising the steps of:
a) providing the fluorinated sulfate salt and the polytrimethylene terephthalate;
b) mixing the polytrimethylene terephthalate and the fluorinated sulfate salt to form a mixture; and
c) heating and blending the mixture with agitation to form the composition.
17. The process of claim 16, wherein step (c) occurs at about 1800C to about 2700C.
18. An article made from the polytrimethylene terephthalate-based composition of claim 1.
19. The article of claim 18, that is in the form of a fiber.
PCT/US2008/072174 2007-08-06 2008-08-05 Flame retardant polytrimethylene terephthalate composition WO2009020946A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013079383A1 (en) * 2011-11-28 2013-06-06 Solvay Specialty Polymers Usa, Llc Polymer composition

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8021736B2 (en) * 2006-07-13 2011-09-20 E.I. Du Pont De Nemours And Company Substantially flame retardant-free 3GT carpet
US20100159186A1 (en) * 2008-12-18 2010-06-24 E. I. Du Pont De Nemours And Company Poly-trimethylene terephthalate solid core fibrillation-resistant filament having a substantially triangular cross section, a spinneret for producing the filament, and a carpet made therefrom
US20110039467A1 (en) * 2009-08-11 2011-02-17 H&C Chemical Ionic liquid flame retardants
US8604105B2 (en) 2010-09-03 2013-12-10 Eastman Chemical Company Flame retardant copolyester compositions

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004035672A1 (en) * 2002-10-14 2004-04-29 Bayer Materialscience Ag Flameproof polycarbonates and polyester carbonates
EP1462503A1 (en) * 2001-12-06 2004-09-29 DAICEL CHEMICAL INDUSTRIES, Ltd. Flame retardant composition, process for producing the same, flame-retardant resin composition, and molded object thereof
EP1630203A1 (en) * 2003-05-26 2006-03-01 Harashina, Hatsuhiko, Polyplastics Co., Ltd. Flame-retardant resin composition

Family Cites Families (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2403207A (en) * 1943-03-08 1946-07-02 Du Pont Chemical process and products
US4203888A (en) * 1974-03-05 1980-05-20 Ici Americas Inc. Polyester films
US4131594A (en) * 1974-05-25 1978-12-26 Teijin Limited Fire-resistant thermoplastic polyester resin compositions and process for rendering polyesters fire-resistant
TW288052B (en) * 1994-06-30 1996-10-11 Du Pont
DE4430932A1 (en) * 1994-08-31 1996-03-07 Hoechst Ag Flame retardant polyester molding compound
US5633362A (en) * 1995-05-12 1997-05-27 E. I. Du Pont De Nemours And Company Production of 1,3-propanediol from glycerol by recombinant bacteria expressing recombinant diol dehydratase
US5686276A (en) * 1995-05-12 1997-11-11 E. I. Du Pont De Nemours And Company Bioconversion of a fermentable carbon source to 1,3-propanediol by a single microorganism
DE19614424A1 (en) * 1996-04-12 1997-10-16 Hoechst Ag Synergistic combination of flame retardants for polymers
US5847616A (en) * 1996-12-12 1998-12-08 Tritech Microelectronics International, Ltd. Embedded voltage controlled oscillator with minimum sensitivity to process and supply
FR2763331B1 (en) * 1997-05-16 1999-06-25 Rhodia Chimie Sa PROCESS FOR THE SYNTHESIS OF SULFONIMIDES AND THEIR SALTS
JPH1121434A (en) * 1997-07-04 1999-01-26 Kanegafuchi Chem Ind Co Ltd Flame retardant thermoplastic resin composition
EP1388546B1 (en) * 1997-07-25 2010-09-08 ACEP Inc. Use of ionic compounds having a delocalised anionic charge as catalyst components
JPH11181255A (en) * 1997-12-18 1999-07-06 Kanegafuchi Chem Ind Co Ltd Thermoplastic resin composition
EP1024167B1 (en) * 1999-01-30 2005-12-21 Clariant GmbH Combination of flame retardants for thermoplastic polymers
US6252111B1 (en) * 1999-02-16 2001-06-26 Central Glass Company, Limited Method for producing sulfonimide or its salt
DE19907831A1 (en) * 1999-02-24 2000-08-31 Bayer Ag Flame-retardant thermoplastic molding compound
US6277947B1 (en) * 2000-04-21 2001-08-21 Shell Oil Company Process of producing polytrimethylene terephthalate (PTT)
DE19933901A1 (en) * 1999-07-22 2001-02-01 Clariant Gmbh Flame retardant combination
US6576309B2 (en) * 1999-12-02 2003-06-10 Associated Packaging Enterprises Thermoplastic compositions having high dimensional stability
US6353062B1 (en) * 2000-02-11 2002-03-05 E. I. Du Pont De Nemours And Company Continuous process for producing poly(trimethylene terephthalate)
TR200201959T2 (en) * 2000-02-11 2003-02-21 E.I.Du Pont De Nemours And Company The process of producing continuous poly (trimethylene terephthalate).
US6685859B2 (en) * 2000-03-03 2004-02-03 E. I. Du Pont De Nemours And Company Processes for making poly(trimethylene terephthalate) yarn
US6752945B2 (en) * 2000-09-12 2004-06-22 E. I. Du Pont De Nemours And Company Process for making poly(trimethylene terephthalate) staple fibers
DE10064335A1 (en) * 2000-12-21 2002-07-04 Degussa Easy flowing polyester molding compound
US6518347B1 (en) * 2000-12-27 2003-02-11 3M Innovative Properties Company Flame retardant carbonate polymers and use thereof
US6657044B1 (en) * 2001-10-30 2003-12-02 Shell Oil Company Process for making polytrimethylene terephthalate
US6613824B2 (en) * 2001-11-12 2003-09-02 General Electric Company Flame retardant resinous compositions and method
US20030175522A1 (en) * 2002-03-13 2003-09-18 Kurian Joseph Varapadavil Poly(trimethylene terephthalate) carpets
DE10309622A1 (en) * 2003-03-04 2004-09-23 Clariant Gmbh Meltable zinc phosphinates
US7084311B2 (en) * 2003-05-06 2006-08-01 E. I. Du Pont De Nemours And Company Hydrogenation of chemically derived 1,3-propanediol
EP2239334A1 (en) * 2003-05-06 2010-10-13 E. I. du Pont de Nemours and Company Purification of biologically-produced 1,3-propanediol
CA2522774A1 (en) * 2003-05-06 2004-11-25 E. I. Du Pont De Nemours And Company Hydrogenation of biochemically derived 1,3-propanediol
KR20070112167A (en) * 2005-03-11 2007-11-22 다이하치 카가쿠 고교 가부시키가이샤 Flame-retardant polyester fiber and method for producing same
JP4784164B2 (en) * 2005-06-15 2011-10-05 三菱エンジニアリングプラスチックス株式会社 Flame retardant polycarbonate resin composition and molded body using the same
US7544813B2 (en) * 2005-09-22 2009-06-09 E.I. Du Pont De Nemours And Company Ionic liquids
JP4996843B2 (en) * 2005-10-28 2012-08-08 ポリプラスチックス株式会社 Flame retardant resin composition
US7531617B2 (en) * 2005-12-21 2009-05-12 E. I. Du Pont De Nemours And Company Continuous process for producing poly(trimethylene terephthalate)

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1462503A1 (en) * 2001-12-06 2004-09-29 DAICEL CHEMICAL INDUSTRIES, Ltd. Flame retardant composition, process for producing the same, flame-retardant resin composition, and molded object thereof
WO2004035672A1 (en) * 2002-10-14 2004-04-29 Bayer Materialscience Ag Flameproof polycarbonates and polyester carbonates
EP1630203A1 (en) * 2003-05-26 2006-03-01 Harashina, Hatsuhiko, Polyplastics Co., Ltd. Flame-retardant resin composition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2013079383A1 (en) * 2011-11-28 2013-06-06 Solvay Specialty Polymers Usa, Llc Polymer composition

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