EP2542622A1 - Composition de polymère de carbonate ignifuge à écoulement amélioré - Google Patents

Composition de polymère de carbonate ignifuge à écoulement amélioré

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Publication number
EP2542622A1
EP2542622A1 EP11706760A EP11706760A EP2542622A1 EP 2542622 A1 EP2542622 A1 EP 2542622A1 EP 11706760 A EP11706760 A EP 11706760A EP 11706760 A EP11706760 A EP 11706760A EP 2542622 A1 EP2542622 A1 EP 2542622A1
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EP
European Patent Office
Prior art keywords
weight
polymer
parts
ignition resistant
polymer composition
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Ceased
Application number
EP11706760A
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German (de)
English (en)
Inventor
Pascal E.R.E.J LAKEMAN
Nuffel Claude Van
Giacomo Parisi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Trinseo Europe GmbH
Original Assignee
Styron Europe GmbH
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Filing date
Publication date
Application filed by Styron Europe GmbH filed Critical Styron Europe GmbH
Publication of EP2542622A1 publication Critical patent/EP2542622A1/fr
Ceased legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K21/00—Fireproofing materials
    • C09K21/06—Organic materials
    • C09K21/12—Organic materials containing phosphorus
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L69/00—Compositions of polycarbonates; Compositions of derivatives of polycarbonates
    • 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
    • C08K5/00—Use of organic ingredients
    • C08K5/49—Phosphorus-containing compounds
    • C08K5/51—Phosphorus bound to oxygen
    • C08K5/52—Phosphorus bound to oxygen only
    • C08K5/521—Esters of phosphoric acids, e.g. of H3PO4
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2205/00—Polymer mixtures characterised by other features
    • C08L2205/03—Polymer mixtures characterised by other features containing three or more polymers in a blend
    • 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
    • C08L25/02—Homopolymers or copolymers of hydrocarbons
    • C08L25/04—Homopolymers or copolymers of styrene
    • C08L25/08—Copolymers of styrene
    • C08L25/12—Copolymers of styrene with unsaturated nitriles
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L27/00—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 a halogen; Compositions of derivatives of such polymers
    • C08L27/02—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 a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L27/12—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 a halogen; Compositions of derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L51/00—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers
    • C08L51/04—Compositions of graft polymers in which the grafted component is obtained by reactions only involving carbon-to-carbon unsaturated bonds; Compositions of derivatives of such polymers grafted on to rubbers
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L55/00—Compositions of homopolymers or copolymers, obtained by polymerisation reactions only involving carbon-to-carbon unsaturated bonds, not provided for in groups C08L23/00 - C08L53/00
    • C08L55/02—ABS [Acrylonitrile-Butadiene-Styrene] polymers
    • 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

Definitions

  • the present invention relates to an ignition resistant carbonate polymer composition demonstrating improved flow characteristics.
  • Said composition comprises a polycarbonate (PC); a mass polymerized graft (co)polymer, preferably a mass polymerized acrylonitrile, butadiene, and styrene terpolymer (mABS); a polyalkylene dicarboxylate polymer, preferably a low viscosity thermoplastic semi-crystalline polyester (PES); and an anti drip agent comprising a polytetrafluoroethylene polymer, a fluorothermoplast, or mixture thereof.
  • the present invention further relates to a method to make said improved flow ignition resistant carbonate polymer composition and fabricated articles formed therefrom.
  • Underwriter's Laboratories typically need to meet flammability requirements from one or more regulatory agency, for example Underwriter's Laboratories.
  • Underwriter's Laboratories Standard 94 UL 94
  • UL 94 Underwriter's Laboratories Standard 94
  • Carbonate polymer compositions are not inherently ignition resistant. A variety of techniques have been disclosed which help to meet industry requirements by imparting ignition resistance and lowering the ease in which a carbonate polymer composition catches on fire.
  • non-halogen phosphorus flame retardant additives have been employed in carbonate polymer compositions to improve ignition resistance by gas phase mechanisms (as a free radical scavenger).
  • gas phase mechanisms as a free radical scavenger
  • attempts to further minimize the ease of flammability by solid phase mechanisms e.g., char forming
  • carbonate compositions, being thermoplastic are predisposed to softening and dripping when heated. To minimize dripping, the viscosity of the carbonate polymer can be lowered so it does not flow easily and/or a drip suppressant such as polytetrafluoroethane (PTFE) is employed.
  • PTFE polytetrafluoroethane
  • Ignition resistant carbonate polymer compositions are well known, for example see USP 5,061,745; 6,596,794; 6,727,301; 6,753,366; and Re 36,188. These patents describe compositions comprising a carbonate polymer, a graft (co)polymer, a phosphorus compound, and polytetrafluoroethane.
  • a key challenge in providing a useful ignition resistant carbonate polymer composition is that typically the ignition resistant additive(s) and/or techniques which impart the desired ignition resistant performance cause detrimental effects with one or more of the carbonate composition's other properties, for instance mechanical properties (notably brittleness), thermal properties (thermal instability due to the heat generated by the electronics), aesthetic properties (such as pitting, streaking, gloss gradients, etc.), and especially processability (thus limiting the ability to make thin and/or large parts).
  • the present invention is such an ignition resistant carbonate polymer composition.
  • the ignition resistant carbonate polymer composition of the present invention comprises: (i) an aromatic polycarbonate or an aromatic polyester carbonate, (ii) a graft (co)polymer produced by mass polymerization, (iii) a thermoplastic semi-crystalline polyalkylene dicarboxylate polymer having an intrinsic viscosity of from 0.4 to 0.7 dl/g, (iv) an aromatic phosphorous com und represented by the formula I:
  • R 1 , R 2 , R 3 and R 4 independently of one another each denote optionally halogenated Ci- to Ce-alkyl, or C5- to C6- cycloalkyl, C - to C20- aryl or C 7 - to C12- aralkyl, in each case optionally substituted by alkyl and/or halogen
  • X denotes a mono- or polynuclear aromatic radical having 6 to 30 C atoms
  • n independently of one another is 0 or 1
  • N represents values from 0 to 30,
  • a polytetrafluoroethylene polymer, fluorothermoplast, or mixture thereof and (vi) one or more of a thermoplastic vinyl (co)polymer, an impact modifier, a filler, a reinforcing material, a stabilizer, a pigment, a dye, a mold release agent, a lubricant, or an anti-static agent.
  • component (i) in the hereinabove composition is present in an amount from 30 to 75 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • component (ii) in the hereinabove composition is present in . an amount from 5 to 60 parts by weight based on the total weight of the ignition resistant carbonate polymer composition and preferably comprises (ii.a) from 5 to 99 percent by weight of a grafting (co)polymer comprising one or more vinyl monomers on (ii.b) from 95 to 1 percent by weight, of one or more a grafting backbone having a glass transition temperature (Tg) of less than 10°C, wherein percents by weight are based on the total weight of component (ii) the graft (co)polymer.
  • component (iii) in the hereinabove composition is present in an amount from 5 to 45 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • component (iv) in the hereinabove composition is present in an amount from 2 to 20 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • component (iv) in the hereinabove composition X is derived from a diol selected from diphenylphenol, bisphenol A, resorcinol or hydroquinone.
  • component (iv) in the hereinabove composition the phosphorous compound comprises a mixture of from 3 to 95 weight percent monophosphate compound of formula I and 97 to 5 weight percent oligomeric phosphate compound of formula I.
  • component (v) in the hereinabove composition the polytetrafluoroethylene polymer, a fluorothermoplast, or mixture thereof is present in an amount of from 0.01 to 5 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • component (v) is a mixture of fibril forming
  • polytetrafluoroethylene polymer and fluorothermoplast present in an amount of from 0.1 to 3 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • component (v) in the hereinabove composition the same
  • fluorothermoplast comprises a polymer of interpolymerized units derived from
  • TFE tetrafluoroethylene
  • HFP hexafluoropropylene
  • VDF vinylidenefluonde
  • R 8 2 C CR 8 2 wherein each of R 8 is independently selected from H, CI, or an alkyl group of from 1 to 8 carbon atoms, a cyclic alkyl group of from 1 to 10 carbon atoms, or an aryl group of from 1 to 8 carbon atoms.
  • component (v) in the hereinabove composition the fluorothermoplast comprises a terpolymer. having interpolymerized units derived from tetrafluoroethylene (TFE), hexafluoropropylene (HFP) and vinylidenefluoride (VDF).
  • TFE tetrafluoroethylene
  • HFP hexafluoropropylene
  • VDF vinylidenefluoride
  • the present invention is a method to make the hereinabove composition comprising the steps of melt-compounding components (i), (ii), (iii), (iv), (v) and (vi).
  • the present invention is a formed article comprising the hereinabove composition
  • the formed article is an interior trim for rail vehicles, an interior and/or exterior automotive article, an enclosure for electrical devices containing small transformers, an enclosure for information dissemination and/or transmission device, an enclosure and/or cladding for medical purposes, a message device and/or enclosures therefore, a toy vehicles for children, a sheet wall element, an enclosure for safety equipment, a hatchback spoiler, a thermally insulated transport container, an apparatus for keeping and/or caring for small animals, an article for sanitary and/or bathroom installations, a cover grill for ventilation openings, an article for summer houses and sheds, and/or enclosures for garden appliances.
  • Preferred fabricated articles include an instrument housing or enclosure such as for: a power tool, an appliance, a consumer electronic equipment such as a TV, a VCR, a DVD player, a web appliance, an electronic book, etc., - or an enclosure for. information technology equipment such as a telephone, a computer, a monitor, a fax machine, a battery charger, a scanner, a copier, a printer, a hand held computer, a flat screen display, and the like.
  • Component (i) of the present invention is a thermoplastic aromatic polycarbonate and/or aromatic polyester carbonate.
  • Suitable aromatic polycarbonates and/or aromatic polyester carbonates according to the invention are known from the literature or can be produced by methods known from the literature (for example, for the production of aromatic polycarbonates, see Schnell, "Chemistry and Physics of Polycarbonates",
  • aromatic polycarbonates is effected, for example, by the reaction of diphenols with carbonic acid halides, preferably phosgene, and/or with aromatic dicarboxylic acid dihalides, preferably benzenedicarboxylic acid dihalides, by the phase boundary method, optionally with the use of chain terminators, e.g., monophenols, and optionally with the use of trifunctional branching agents or branching agents with a functionality higher than three, for example triphenols or tetraphenols.
  • chain terminators e.g., monophenols
  • trifunctional branching agents or branching agents with a functionality higher than three for example triphenols or tetraphenols.
  • Diphenols for the production of the aromatic polycarbonates and/or aromatic polyester carbonates are referably those of formula ⁇
  • A denotes a single bond, a Q - C5 alkylene, a C 2 - C5 alkylidene, a C5 - C cycloalkylidene, -0-, -SO-, -CO-, -S-, -SO2-, or a Ce - Q 2 arylene, on to which other aromatic rings, which optionally contain hetero atoms, can be condensed, or a radical of formula ⁇ or IV
  • B in each case is independently hydrogen, a Q - C12 alkyl, preferably methyl, or a halogen, preferably chlorine and/or bromine;
  • x in each case is mutually independently 0, 1, or 2;
  • p is 0 or 1 ;
  • R c and R d are mutually independent of each other and are individually selectable for each X 1 and are hydrogen or a Ci - Ce alkyl, preferably hydrogen, methyl or ethyl; X 1 denotes carbon; and
  • n denotes an integer from 4 to 7, preferably 4 or 5, with the proviso that R° and R d simultaneously denotes an alkyl on at least one Xi atom.
  • the preferred diphenols are hydroquinone, resorcinol, dihydroxybiphenyls, bis(hydroxyphenyl)-Ci - C5 alkanes, bis(hydroxyphenyl)-C5 -Q cycloalkanes,
  • bis(hydroxyphenyl)ethers bis(hydroxyphenyl)sulfoxides, bis(hydroxyphenyl)ketones, bis(hydroxyphenyl)sulfones and alpha, alpha'-bis(hydroxyphenyl)diisopropylbenzenes, as well as derivatives thereof which have brominated and/or chlorinated nuclei.
  • Diphenols which are particularly preferred are 4,4'-dihydroxybiphenyl, bisphenol A, 2,4-bis(4-hydroxyphenyl)-2-methylbutane, 1 , 1 -bis(4-hydroxyphenyl)-cyclohexane, 1,1- bis(4-hydroxyphenyl)-3,3,5-trimethylcyclohexane, 4,4-dihydroxydiphenyl sulfide and 4,4- dihydroxydiphenyl sulfone, as well as di- and tetrabrominated or chlorinated derivatives thereof, such as 2,2-bis(3-chloro-4-hydroxyphenyl)propane, 2,2-bis-(3,5-dichloro-4- hydroxyphenyl)propane or 2,2-bis(3,5-dibrorao-4-hydroxyphenyl)propane.
  • 2, 2-bis-(4- hydroxyphenyl)propane (bisphenol A) is particularly preferred.
  • the diphenols can be used individually or as
  • chain terminators for the production of the aromatic polycarbonates include phenol, p-chlorophenol, p-tert-butylphenol or 2,4,6-tribromophenol, as well as long chain alkylphenols such as 4-(l,3-dimethyl-butyl)-phenol or
  • monoalkylphenols or dialkylphenols which contain a total of 8 to 20 C atoms in their alkyl substituents, such as 3,5-di-tert-butyl-phenol, p-iso-octylphenol, p-tert-octylphenol, p- dodecylphenol, 2-(3,5-dimethylheptyl)-phenol and 4-(3,5-dimethylheptyl)-phenol.
  • the amount of chain terminators used is generally between 0.1 mole percent and 10 mole percent with respect to the molar sum of the diphenols used in each case.
  • the aromatic polycarbonates and/or aromatic polyester carbonates of the present invention preferably have a mean weight average molecular weights of from about 10,000 to about 200,000 preferably about 20,000 to about 80,000.
  • molecular weight herein refer to weight average molecular weights (M w ) determined by gel permeation chromatography (GPC) using laser scattering techniques with a bisphenol A polycarbonate standard and is given in units of grams per mole (g/mole).
  • the aromatic polycarbonates can be branched in the known manner, for example by the incorporation of 0.05 to 2.0 mole percent, with respect to the sum of the diphenols used, of trifunctional compounds or of compounds with a functionality higher than three, for example those which contain three or more phenolic groups.
  • Branched polycarbonates suitable for the present invention can be prepared by known techniques, for example several suitable methods are disclosed in USP 3,028,365; 4,529,791 ; and 4,677, 162; which are hereby incorporated by reference in their entirety.
  • Suitable branching agents that may be used are tri- or multi-functional carboxylic acid chlorides, such as trimesic acid trichloride, cyanuric acid trichloride, 3,3'- ,4,4'- benzophenonetetracarboxylic acid tetrachloride, 1 ,4,5,8-naphthalene-tetracarboxylic acid tetrachloride or pyromellitic acid tetrachloride for example, in amounts of 0.01 to 1.0 mole percent (with respect to the dicarboxylic acid dichlorides used) or tri- or multi-functional phenols such as phloroglucinol, 4,6-dimethyl-2,4,6-tris(4-hydroxyphenyl)-2-heptene, 4,4- dimethyl-2,4,6-tris(4-hydroxyphenyl)heptane, l,3,5-tris(4-hydroxyphenyl)benzene, 1,1,1- tris(4-hydroxy
  • copolycarbonates are suitable.
  • 1 to 25 parts by weight, preferably 2.5 to 25 parts by weight (with respect to the total amount of diphenols to be used) of polydiorganosiloxanes comprising hydroxy-aryloxy terminal groups can also be used. These are known (see, for example, USP 3,419,634) or can be produced by methods known from the literature.
  • the preferred polycarbonates are the copolycarbonates of bisphenol A with up to 15 mole percent, with respect to the molar sums of the diphenols, of other diphenols which are cited as preferred or particularly preferred, in particular 2,2-bis(3,5-dibromo-4-hydroxyphenyl)-propane.
  • the preferred aromatic dicarboxylic acid dihalides for the production of the aromatic polyester carbonates are the diacid dichlorides of isophthalic acid, terephthalic acid, diphenyl ether-4,4'-dicarboxylic acid and naphthalene-2,6-dicarboxylic acid. Mixtures of the diacid dichlorides of isophthalic acid and terephthalic in a ratio between 1 :20 and 20: 1 are particularly preferred.
  • a carbonic acid halide, preferably phosgene, is used in conjunction as a difunctional acid derivative during the production of the polyester carbonates.
  • suitable chain terminators for the production of the aromatic polyester carbonates include chlorocarboxylic acid esters thereof, as well as the acid chlorides of aromatic monocarboxylic acids which may optionally be substituted by Ci - C22 alkyl groups, or by halogen atoms, and also include aliphatic C 2 - C 22 monocarboxylic acid chlorides.
  • the amount of chain terminator is 0.1 to 10 mole percent in each case, with respect to the moles of diphenols in the case of phenolic chain terminators and with respect to the moles of dicarboxylic acid dichlorides in the case of monocarboxylic acid chloride chain terminators.
  • the aromatic polyester carbonates may also contain incorporated hydroxycarboxylic acids.
  • the aromatic polyester carbonates may be either linear or may be branched. Suitable branching agents are disclosed hereinabove.
  • the proportion of carbonate structural units in the aromatic polyester carbonates can be arbitrarily varied.
  • the content of carbonate groups is preferably up to 100 mole percent, particularly up to 80 mole percent, most preferably up to 50 mole percent, with respect to the sum of ester groups and carbonate groups.
  • Both the ester and the carbonate fraction of the aromatic polyester carbonates can be present in the form of blocks, or can be randomly distributed in the condensation polymer.
  • the relative solution viscosity ( ⁇ ) of the aromatic polycarbonates and aromatic polyester carbonates is within the range of 1.18 to 1.4, preferably 1.22 to 1.3 (as measured on solutions of 0.5 g of polycarbonate and polyester carbonate, respectively, in 100 mL of methylene chloride at 25°C).
  • aromatic polycarbonates and aromatic polyester carbonates can be used individually or in any mixture with each other.
  • thermoplastic aromatic polycarbonates and/or aromatic polyester carbonates (i) are present in an amount equal to or greater than about 30 parts by weight, preferably equal to or greater than about 35 parts by weight, preferably equal to or greater than about 40 parts by weight, and more preferably equal to or greater than about 45 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • thermoplastic aromatic polycarbonates and/or aromatic polyester carbonates (i) are present in an amount equal to or less than about 75 parts by weight, preferably equal to or greater than about 70 parts by weight, more preferably equal to or greater than about 65 parts by weight, more preferably equal to or greater than about 60 parts by weight, and more preferably equal to or less than about 55 parts by weight based on the weight of the ignition resistant carbonate polymer composition. Unless stated otherwise, parts by weight are based on the total weight of the ignition resistant carbonate polymer composition.
  • Component (ii) of the present invention is a graft (co)polymer, preferably one or more grafting (co)polymer (ii.a) comprising one or more vinyl monomer grafted on one or more grafting backbone (ii.b), said grafting backbone having a glass transition temperature less than 10°C, preferably less than 0°C, preferably less than about -10°C, and more preferably less than -20°C.
  • the grafting backbone (ii.b) generally has an average particle size (Dy, value) of from 0.01 to 7 microns.
  • the grafting (co)polymer (ii.a) is present in an amount of from 5 to 99, preferably 30 to 80 percent by weight and the grafting backbone (ii.b) is present in an amount of from 95 to 1, preferably from 70 to 20 percent by weight, weight percents are based on the total weight of the graft (co)polymer (ii).
  • the grafting copolymer (ii.a) comprises monomers which are preferably mixtures (ii.a.1) of 50 to 99 parts by weight of aromatic vinyl compounds and/or aromatic vinyl compounds with substituted nuclei (such as styrene, alpha-methylstyrene, p- methylstyrene or p-chlorostyrene) and or butylacrylate, ethylacrylate, or ethylhexylacrylate and/or Q - C alkyl esters of (meth)acrylic acid (such as methyl methacrylate or ethyl methacrylate), and (ii.a.2) 1 to 50 parts by weight of vinyl cyanides (unsaturated nitriles, such as acrylonitrile and methacrylonitrile) and/or C ⁇ - C 4 alkyl esters of (meth)acrylic acid (such as methyl methacrylate, n-butyl acrylate and
  • monomers
  • the preferred monomers are selected from at least one of the monomers styrene, alpha-methylstyrene and methyl methacrylate.
  • the preferred monomers (ii.a.2) are selected from at least one of the monomers acrylonitrile, maleic anhydride and methyl methacrylate.
  • the monomers which are particularly preferred are styrene as (ii.a.l) and acrylonitrile as (ii.a.2).
  • Suitable grafting backbones (ii.b) for graft (co)polymers (ii) include diene rubbers, ethylene/propylene and optionally diene (EP(D)M) rubbers, acrylate, polyurethane, silicone, silicone/acrylate, chloroprene and ethylene/vinyl acetate rubbers.
  • the preferred grafting backbones (ii.b) are diene rubbers (for example based on butadiene, isoprene, etc.) or mixtures of diene rubbers or copolymers of diene rubbers or mixtures thereof with other copolymerizable monomers (for example according to (ii.a.l) and (ii.a.2)), providing that the glass transition temperature is less than about 10°C, preferably less than about 0°C, preferably less than about -10°C, and more preferably less than about -20°C. Pure polybutadiene rubber is particularly preferred.
  • a particularly preferred graft (co)polymer (ii) is acrylonitrile, butadiene, and styrene terpolymer (ABS).
  • Graft (co)polymers (ii) are produced by radical polymerization, for example by emulsion, mass, suspension, solution or bulk polymerization.
  • radical polymerization for example by emulsion, mass, suspension, solution or bulk polymerization.
  • mass-solution sometimes referred to as solution
  • mass-suspension sometimes referred to as suspension
  • ABS polymers may be produced by redox initiation with an initiator system comprising an organic hydroperoxide and ascorbic acid according to USP 4,937,285; which is incorporated herein by reference.
  • the ignition resistant carbonate polymer composition of the present invention we found that using a mass polymerized non-silicon-containing graft (co)polymer is most preferred. A mixture of mass and emulsion polymerized non-silicon-containing graft (co)polymer is less preferred, but may still result in an acceptable overall balance of properties. However, we have found that for the ignition resistant carbonate polymer compositions of the present invention, the use of emulsion polymerized non-silicon- containing graft (co)polymer will not achieve an acceptable balance of properties, especially in regards to hydrolytic stability.
  • Suitable acrylate rubbers according to (ii.b) of graft (co)polymer (ii) are preferably polymers of acrylic acid alkyl esters, optionally with up to 40 percent by weight, with respect to (ii.b), of other polymerizable, ethylenically unsaturated monomers.
  • the preferred polymerizable acrylic acid esters include C ⁇ - C 8 alkyl esters, for example methyl, ethyl, butyl, n-octyl and 2-ethylhexyl esters: halogenoalkyl esters, preferably halogeno-Ci - Ce - alkyl esters such as chloroethyl acrylate, as well as mixtures of these monomers.
  • Monomers with more than one polymerizable double bond can be copolymerized to provide cross-linking.
  • the preferred examples of cross-linking monomers are the esters of unsaturated monocarboxylic acids containing 3 to 8 C atoms and unsaturated monohydric alcohols containing 3 to 12 C atoms, or saturated polyols containing 2 to 4 OH groups and 2 to 20 C atoms, such as ethylene glycol dimethacrylate or allyl methacrylate for example; multiply-unsaturated heterocyclic compounds, such as trivinyl and triallyl cyanurate for example; polyfunctional vinyl compounds such as di- and trivinylbenzenes; and also triallyl phosphate and diallyl phthalate.
  • the preferred cross-linking monomers are allyl methacrylate, ethylene glycol dimethacrylate, diallyl phthalate and heterocyclic compounds which contain at least 3 ethylenically unsaturated groups.
  • Cross-linking monomers which are particularly preferred are the cyclic monomers triallyl cyanurate, triallyl isocyanurate, triacryloyl hexahydro-s- triazine and triallylbenzenes.
  • the amount of cross-linked monomer is preferably 0.02 to 5, particularly 0.05 to 2 percent by weight, with respect to grafting backbone (ii.b).
  • grafting backbone ii.b
  • graft base examples include acrylonitrile, styrene, alpha-methylstyrene, acrylamides, vinyl-Ci - C1 ⁇ 4- alkyl ethers, methyl methacrylate and butadiene.
  • the acrylate rubbers which are preferred as the grafting backbone (ii.b) are emulsion polymers which have a gel content of at least 20 percent, preferably 40 percent, more preferably 60 percent by weight.
  • grafting backbones which are suitable according to (ii.b) are silicone rubbers with graft-active sites.
  • graft (co)polymers (ii) are also to be understood according to the invention to include those products which are obtained by (co)polymerization of the graft monomers in the presence of the graft base and which occur in conjunction during processing (i.e., (co)polymer from the polymerization of graft monomer(s) of (ii.a)).
  • the average graft base particle size is a volume-weighted mean particle diameter (D v ) determined by analyzing Transmission Electron Microscopy (TEM) images, for a good discussion of particle size determination see USP 6,380,304 which is incorporated herein by reference.
  • D v volume-weighted mean particle diameter
  • USP 6,380,304 which is incorporated herein by reference.
  • a correction for section thickness is done when particles are larger than 1 micron.
  • the average particle diameter of the grafting backbone (ii.b) produced by a mass process is equal to or greater than about 0.01 microns, preferably equal to or greater than about 0.1 microns, more preferably equal to or greater than about 0.2 microns, and even more preferably equal to or greater than about 0.3 microns.
  • the average particle diameter of the grafting backbone (ii.b) produced by a mass process is equal to or less than about 7 microns, preferably equal to or less than about 6 microns, more preferably equal to or less than about 5 microns, and even more preferably equal to or less than about 4 microns.
  • the rubber-modified polymers of the present invention can have a broad
  • the rubber components can comprise one rubber or a blend of rubbers.
  • more than one rubber can be used in a
  • a bimodal rubber particle size distribution is defined as having two distinct peaks of particles when graphed on axes of particle size versus volume fraction, whereby one peak designates smaller particles and the other peak designates larger particles.
  • the larger particle fraction will have a volume average particle size of from about 0.5 microns, and most preferably from about 0.7 microns to about 3 microns, preferably to about 2.5 microns, and most preferably to about 2 microns.
  • the smaller particle fraction will have a volume average particle size of from about 0.01 microns, preferably from about 0.1 microns to 0.4 microns, preferably to about 0.35 microns, and more preferably to about 0.3 microns.
  • the gel content of grafting backbone (ii.b) produced by a mass process can be determined at 25°C in toluene and is at least 10 weight percent, preferably at least 15 weight percent, even more preferably at lest 20 weight percent, and most preferably at least 25 weight percent based on the total weight of the grafting backbone (ii.b).
  • the average particle diameter of the grafting backbone (ii.b) produced by an emulsion process is equal to or greater than about 0.01 microns, preferably equal to or greater than about 0.03 microns, and even more preferably equal to or greater than about 0.05 microns.
  • the average particle diameter of the grafting backbone (ii.b) produced by an emulsion process is equal to or less than about 2 microns, preferably equal to or less than about 1.5 microns, and even more preferably equal to or less than about 1 micron.
  • the larger particle fraction will have a volume average particle size of from about 0.3 microns, more preferably from about 0.4 microns, and most preferably from about 0.5 microns to about 3 microns, preferably to about 2 microns, more preferably to about 1.5 microns, and most preferably to about 1 micron.
  • the smaller particle fraction will have a volume average particle size of from about 0.01 microns, preferably from about 0.03 microns to 0.3 microns, preferably from about 0.05 microns to about 0.2 microns.
  • the gel content of an emulsion produced grafting backbone is at least 20 percent by weight, preferably at least 30 percent, more preferably at least 40 percent, even more preferably at least 50 percent, and most preferably at least 60 percent by weight as measured in toluene.
  • the average particle diameter of the grafting backbone (ii.b) is equal to or greater than about 0.01 microns, preferably equal to or greater than about 0.1 microns, more preferably equal to or greater than about 0.15 microns, more preferably equal to or greater than about 0.2 microns, and even more preferably equal to or greater than about 0.25 microns.
  • the average particle diameter of the grafting backbone (ii.b) is equal to or less than about 7 microns, preferably equal to or less than about 5 microns, more preferably equal to or less than about 4 microns, more preferably equal to or less than about 3 micron, and most preferably equal to or less than 2 microns.
  • the resulting bimodal rubber particle size distribution may be described by the independent preferred rubber particle size ranges given hereinabove for mass produced graft polymer and emulsion produced graft polymer.
  • the graft (co)polymer (ii) is present in an amount equal to or greater than about 5 parts by weight, preferably equal to or greater than about 7 parts by weight, more preferably equal to or greater than about 10 parts by weight, and more preferably equal to or greater than about 12 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • the graft (co)polymer (ii) is present in an amount equal to or less than about 60 parts by weight, preferably equal to or less than about 50 parts by weight, more preferably equal to or less than about 40 parts by weight, more preferably equal to or less than about 30 parts by weight, and more preferably equal to or less than about 25 parts by weight based on the total weight of the ignition resistant carbonate polymer composition.
  • Component (iii) of the present invention comprises a thermoplastic polyalkylene dicarboxylate polymer, commonly referred to as a polyester.
  • a thermoplastic polyalkylene dicarboxylate polymer commonly referred to as a polyester.
  • Preferable thermoplastic polyalkylene dicarboxylate polymers are semi-crystalline, preferably made by melt polymerization having, and more preferably having a low molecular weight.
  • Suitable thermoplastic polyalkylene dicarboxylate polymers are reaction products of aromatic dicarboxylic acids or the reactive derivatives thereof, such as dimethyl esters or anhydrides, and aliphatic, cycloaliphatic or araliphatic diols, dialkyl esters, diacid chlorides, carboxylic acid salts, and diaryl esters, together with mixtures of these reaction products.
  • the dicarboxylic acid may be an aliphatic acid such as succinic, glutaric, adipic, sebacic, azelaic, suberic acid, or cyclohexane dicarboxylic acid, or an aromatic acid such as isophtalic acid, terephthalic acid, naphthyl dicarboxylic acid, or biphenyl dicarboxylic acid.
  • the aromatic acids, especially terephthalic acid are preferred.
  • the use of an ester and especially a lower alkyl ester is preferred, more preferably a methyl, ethyl or butyl ester.
  • Preferred polyalkylene dicarboxylate polymers are produced using a mole ratio of diol component to dicarboxylic acid or ester component from about 1 : 1 to about 1.4: 1 and preferably from about 1.2:1 to about 1.3:1.
  • the preferred polyalkylene dicarboxylate may contain up to 20 mole percent, preferably up to 10 mole percent, of residues of other aromatic or cycloaliphatic dicarboxylic acids having 8 to 14 C atoms or aliphatic
  • dicarboxylic acids having 4 to 12 C atoms such as for example residues of phthalic acid, isophthalic acid, 2,6-naphthalenedicarboxylic acid, 4,4'-diphenyldicarboxylic acid, succinic acid, adipic acid, sebacic acid, azelaic acid, cyclohexanediacetic acid.
  • the preferred polyalkylene dicarboxylate polymers may contain up to 20 mole percent, preferably up to 10 mole percent, of other aliphatic diols having 3 to 12 C atoms or cycloaliphatic diols having 6 to 21 C atoms, for example residues of 1,3-propanediol, 2-ethyl-l,3-propanediol, neopentyl glycol, 1,5-pentanediol, 1,6-hexanediol, 1,4-cyclohexanedimethanol, 3-ethyl-2,4-pentane- diol, 2-methyl-2,4-pentanediol, 2,2,4-trimethyl-l,3-pentanediol, 2-ethyl-l,3-hexane-diol, 2,2-diethyl- 1,3-propan
  • the polyalkylene dicarboxylate polymers may be branched by incorporating relatively small quantifies of tri-. or tetrahydric alcohols or tri- or tetrabasic carboxylic acids, for example according to USP 3,692,744.
  • further preferred branching agents are trimesic acid, trimellitic acid, trimethylolethane and trimethylolpropane and
  • Particularly preferred polyalkylene dicarboxylate polymers are those solely produced from terephthalic acid and the reactive derivatives thereof (for example the dialkyl esters thereof) and ethylene glycol (such as polyethylene terephthalate (PET)) and/or 1, 4- butanediol (such as polybutylene terephthalate (PBT)), and mixtures of these polyalkylene terephthalate polymers.
  • terephthalic acid and the reactive derivatives thereof for example the dialkyl esters thereof
  • ethylene glycol such as polyethylene terephthalate (PET)
  • PBT polybutylene terephthalate
  • Preferred mixtures of polyalkylene dicarboxylate polymers contain 1 to 50 weight percent, preferably 1 to 30 weight percent, of polyethylene terephthalate polymer and 50 to 99 weight percent, preferably 70 to 99 weight percent, of polybutylene terephthalate polymer.
  • Polyalkylene dicarboxylate polymers may be made by melt polymerization and/or solid- state polymerization.
  • the polyalkylene dicarboxylate polymer of the present invention desirably is made by melt polymerization and has a low molecular weight, for example see USP 5,714,262 which is incorporated by reference herein in its entirety.
  • the molecular weight of a polyalkylene dicarboxylate polymer is reflected in its intrinsic viscosity (IV) which is expresses in deciliters per gram (dl/g); the higher the molecular weight (longer the polymer chains), the stiffer the material and, consequently, the higher the intrinsic viscosity.
  • the intrinsic viscosity for the polyalkylene dicarboxylate polymers used in the carbonate polymer compositions of the present invention preferably have an intrinsic viscosity of from 0.4 to 0.7 dl/g, more preferably of from 0.5 to 0.6 dl/g measured in phenol/o- dichlorobenzene (1:1 parts by weight) at 25 °C in an Ubbelohde viscosimeter.
  • the polyalkylene dicarboxylate polymers may be produced using known methods.
  • the reaction between the alkanediol and the dicarboxylic acid is typically promoted by a metallic catalyst; useful catalysts in the preparation of polyesters are described, for example in USP 4,401,804, incorporated herein by reference. Further suitable reagents for forming polyesters are described, for example, in the following USP 2,465,319; 2,720,502;
  • a preparation example of described polyalkylene dicarboxylate polymers could entail heating the dicarboxylic acid or ester thereof, alkenediol and metallic catalyst to typically 180°C-300°C for a period of time suitable for producing the desired polymer.
  • the amount of metallic catalyst used is typically about 0.005-0.2 percent by weight, based on the amount of acid or ester.
  • thermoplastic semi-crystalline polyalkylene dicarboxylate polymer (iii) is present in an amount equal to or greater than about 5 parts by weight, preferably equal to or greater than about 10 parts by weight, more preferably equal to or greater than about 15 parts by weight, and more preferably equal to or greater than about 20 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • thermoplastic polyalkylene dicarboxylate polymer (iii) is present in an amount equal to or less than about 45 parts by weight, preferably equal to or less than about 40 parts by weight, more preferably equal to or less than about 35 parts by weight, more preferably equal to or less than about 30 parts by weight, and more preferably equal to or less than about 25 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • Component (iv) of the present invention is an aromatic phosphorous compound that has the formula I:
  • R 1 , R 2 , R 3 and R 4 independently of one another each denote optionally halogenated Ci- to Cg-alkyl, or C5- to Q- cycloalkyl, Ce- to C 2 o- aryl or C7- to C12- aralkyl, in each case optionally substituted by alkyl, preferably Ci-C 4 -alkyl, and/or halogen, preferably bromine or chlorine.
  • R 1 , R 2 , R 3 and R 4 independently of one another represent C1-C4 -alkyl, phenyl, naphthyl or phenyl-C
  • aromatic groups R 1 , R 2 , R 3 and R 4 can in turn be substituted by halogen and/or alkyl groups, preferably chlorine, bromine and/or Ci-Q-alkyl.
  • Particularly preferred aryl radicals are cresyl, phenyl, xylenyl, propylphenyl or butylphenyl and the corresponding brominated and chlorinated derivatives thereof.
  • X in the formula I denotes a mono- or polynuclear aromatic radical having 6 to 30 C atoms. This is derived from diphenols of the formula ⁇ . Preferred diphenols are diphenylphenol, bisphenol A, resorcinol or hydroquinone or chlorinated or brominated derivatives thereof,
  • n in the formula I independently of one another can be 0 or 1 , and n is preferably 1.
  • N represents values from 0 to 30, preferably an average value of 0.3 to 20, particularly preferably 0.5 to 10, in particular 0.5 to 6.
  • R 1 , R 2 , R 3 and R 4 , n and N have the meaning given above in the case of formula I, R 5 and R 6 independently of one another denote Ci-C4-alkyl, preferably methyl, or
  • halogen preferably chlorine and/or bromine
  • Y denotes Ci-C 7 -alkylidene, Ci-C7-alkylene, Cs-Cn-cycloalkylene, C5-C12- cycloalkylidene, --0—,— S— ,—SO— or—CO— and q denotes 0 or the number 1 or 2, and Y preferably represents Ci-C 7 -alkylidene, in particular isopropylidene, or methylene
  • component (iv) is preferably present in the molding
  • compositions according to the invention as a mixture of 1 to 99 weight percent, preferably 3 to 95 weight percent, more preferably 5 to 90 weight percent, more preferably 10 to 90 weight percent, more preferably 12 to 40 weight percent of at least one monophosphorus compound of the formula I and 1 to 99 weight percent, preferably 5 to 97 weight percent, more preferably 10 to 95 weight percent, more 10 to 90 weight percent, more preferably 60 to 88 weight percent of at least one oligophosphorus compound of the formula I, in each case weight percent based on the total weight of phosphorus compounds, and the mixture having an average N of 0.3 to 20, preferably 0.5 to 10, particularly preferably 0.5 to 6.
  • Monophosphorus compounds of the formula I are, in particular, tributyl phosphate, tris-(2-chloroethyl) phosphate, tris-(2,3-dibromopropyl) phosphate, triphenyl phosphate, tricresyl phosphate, diphenyl cresyl phosphate, diphenyl octyl phosphate, diphenyl 2- ethylcresyl phosphate, tri-(isopropylphenyl) phosphate, halogen-substituted aryl phosphates, methylphosphonic acid dimethyl ester, methylphosphonic acid diphenyl ester,
  • phenylphosphonic acid diethyl ester triphenylphosphine oxide or tricresylphosphine oxide.
  • the phosphorus compounds according to component (iv) are known, for example see EP-A 363 608 and EP-A 640 655.
  • the phosphorus compounds (iv) are present in an amount equal to or greater than 2 parts by weight, preferably equal to or greater than 4 part by weight, more preferably equal to or greater than 6 parts by weight, and most preferably equal to or greater than 8 parts by weight based on the total weight of the ignition resistant carbonate polymer composition of the invention.
  • the phosphorus compounds (iv) are present in an amount equal to or less than 30 parts by weight, preferably equal to or less than 25 parts by weight, more preferably equal to or less than 20 parts by weight, and most preferably equal to or less than 15 parts by weight based on the total weight of the ignition resistant carbonate polymer composition of the invention.
  • the anti-drip component (v) of the present invention comprises a
  • polytetrafluoroethylene preferably fibrillating polytetrafluoroethylene, a fluorothermoplast, and/or mixtures thereof.
  • the fibrillating polytetrafluoroethylene is typically a homopolymer of tetrafluoroethylene (TFE) but may also be a copolymer of TFE with for example another fluorinated monomer such as chlorotrifluoroethylene (CTFE), a perfluorinated vinyl ether such as perfluoromethyl vinyl ether (PMVE) or a perfluorinated olefin such as hexafluoropropylene (HFP).
  • CTFE chlorotrifluoroethylene
  • PMVE perfluoromethyl vinyl ether
  • HFP perfluorinated olefin
  • the amount of the fluorinated comonomer should however be low enough so as to obtain a high molecular weight polymer that is not processible from the melt. This means in general that the melt viscosity of the polymer should be more than 10 Pascal seconds (Pa.s.). Typically the amount of the optional comonomers should not be more than 1 percent so that the PTFE conforms to the ISO 12086 standard defining non-melt processible PTFE. Such copolymers of TFE are known in the art as modified PTFE.
  • the fibrillating PTFE typically has an average particle size (number average) of not more than 10 micron. Generally the average particle size of the fibrillating PTFE will be between 50 nanometer and 5 micron, for example between 100 nanometer and 1 micron. A practical range may be from 50 to 500 nanometers. Conveniently, fibrillating PTFE can be produced via aqueous emulsion polymerization.
  • the fluorothermoplast used is typically a semi-crystalline fluoropolymer.
  • the fluorothermoplast should have a melting point such that the fluorothermoplast is in its molten state under the melt processing conditions used for processing the carbonate polymer composition.
  • Fluorothermoplasts having a melting point of 100°C to 310°C are generally desired for use in this invention.
  • the fluorothermoplast has a melting point of between 100°C and 250°C. Frequently, the fluorothermoplast will have a melting point of not more than 225°C.
  • the fluorothermoplast should be used in amount effective to avoid agglomeration of the particles of fibrillating PTFE.
  • the effective amount can be easily determined by one skilled in the art with routine experimentation.
  • an effective amount of fluorothermoplast is an amount of at least 10 percent by weight based on the weight of fibrillating PTFE. It will generally be desired to maximize the amount of PTFE as a higher amount of PTFE will make the latter more effective in achieving desired effects when added to the carbonate polymer composition melt such as for example increasing the melt strength of the carbonate polymer composition.
  • fluorothermoplast is at least 10 percent by weight, for example between 10 and 60 percent by weight, conveniently between 12 and 50 percent by weight, commonly between 15 and 30 percent by weight based on the total weight of fibrillating PTFE.
  • Suitable fluorothermoplasts for use include fluoropolymers that comprise interpolymerized units derived from at least one fluorinated, ethylenically unsaturated monomer, preferably two or more monomers, of the formula V:
  • each R 7 is independently selected from H, F, CI, alkyl of from 1 to 8 carbon atoms, aryl of from 1 to 8 carbon atoms, cyclic alkyl of from 1 to 10 carbon atoms, or perfluoroalkyl of from 1 to 8 carbon atoms.
  • the R group preferably contains from 1 to 3 carbon atoms. In this monomer each R group may be the same as each of the other R groups. Alternatively, each R group may be different from one or more of the other R groups.
  • the fluoropolymer may also comprise a copolymer derived from the
  • each of R 8 is independently selected from H, CI, or an alkyl group of from 1 to 8 carbon atoms, a cyclic alkyl group of from 1 to 10 carbon atoms, or an aryl group of from 1 to 8 carbon atoms.
  • R 8 preferably contains from 1 to 3 carbon atoms.
  • Representative examples of useful fluorinated formula V monomers include, but are not limited to vinylidene fluoride, tetrafluoroethylene, hexafluoropropylene,
  • chlorotrifluoroethylene 2-chloropentafluoropropene
  • dichlorodifluoroethylene 1,1- dichlorofluoroethylene
  • Perfluoro-1, 3-dioxoles may also be used.
  • Representative examples of useful formula VI monomers include ethylene, propylene, etc.
  • fluoropolymers include polyvinylidene fluoride,
  • fluoropolymers derived from the interpolymerization of two or more different formula V monomers and fluoropolymers derived from one or more formula V monomers with one or more formula VI monomers are those having interpolymerized units derived from vinylidene fluoride (VDF) and hexafluoropropylene (HFP); and those derived from tetrafluoroethylene (TFE) and at least 5 weight percent of at least one copolymerizable comonomer other than TFE.
  • This latter class of fluoropolymers includes polymers of interpolymerized units derived from TFE and HFP; polymers of
  • interpolymerized units derived from TFE, HFP and VDF polymers of interpolymerized units derived from TFE, HFP and a formula VI monomer; and polymers derived from interpolymerized units derived from TFE and a formula VI monomer.
  • the fluorothermoplast may be produced by any of the known polymerization techniques although aqueous emulsion polymerization will generally be preferred for obtaining the melt-processible thermoplastic fluoropolymer.
  • Component (v) is preferably prepared by blending an aqueous dispersion of the fibrillating PTFE with an aqueous dispersion of the fluorothermoplast and coagulating the mixed dispersion followed by drying the product.
  • Such a method is disclosed in for example WO 01/27197. Such method offers the advantage that fibrillation of the PTFE is avoided while preparing component (v). It is however also possible to prepare component (v) by dry blending the P FE and the fluorothermoplast.
  • component (v) may contain further adjuvants to obtain particular desired properties.
  • Component (v) comprising a polytetrafluoroethylene, a fluorothermoplast, or mixtures thereof is present in an amount equal to or greater than about 0.01 parts by weight, preferably equal to or greater than about 0.05 parts by weight, more preferably equal to or greater than about 0.1 parts by weight, more preferably equal to or greater than about 0.2 parts by weight, and more preferably equal to or greater than about 0.3 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • Component (v) comprising a polytetrafluoroethylene, a fluorothermoplast, or mixtures thereof is present in an amount equal to or less than about 5 parts by weight, preferably equal to or less than about 3 parts by weight, more preferably equal to or less than about 1 parts by weight, more preferably equal to or less than about 0.8 parts by weight, more preferably equal to or less than about 0.6 parts by weight, and more preferably equal to or less than about 0.5 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • the ignition resistant carbonate polymer compositions according to the invention contains as component (vi) at least one of an additional polymer and/or conventional additive, such as a thermoplastic vinyl (co)polymer, an impact modifier, lubricants and mold release agents, for example low molecular weight ester, pentaerythritol tetrastearate, poly-alpha-olefins, or combinations thereof, nucleating agents, anti-static agents, stabilizers, fillers and reinforcing materials as well as dyes and pigments.
  • an additional polymer and/or conventional additive such as a thermoplastic vinyl (co)polymer, an impact modifier, lubricants and mold release agents, for example low molecular weight ester, pentaerythritol tetrastearate, poly-alpha-olefins, or combinations thereof, nucleating agents, anti-static agents, stabilizers, fillers and reinforcing materials as well as dyes and pigments.
  • Such stabilizers are known in the art, for example see USP 5,922,816; 4,532,290; 4,401,804, all of which are incorporated herein by reference, and may comprise certain phosphorous containing compounds that include phosphoric acid, certain organic phosphorous compounds such as distearyl pentaerythritol diphosphate, mono or dihydrogen phosphate, or mono-, di-, or trihydrogen phosphate compounds, phosphate compounds, and certain inorganic phosphorous compounds such as monosodium phosphate and monopotassium phosphate, silyl phosphates, and silyl phosphate derivatives, alone or in combination and present in an amount effective to inhibit ester-carbonate interchange in the composition.
  • certain organic phosphorous compounds such as distearyl pentaerythritol diphosphate, mono or dihydrogen phosphate, or mono-, di-, or trihydrogen phosphate compounds, phosphate compounds, and certain inorganic phosphorous compounds such as monosodium
  • thermoplastic vinyl (co)polymers are polymers of at least one monomer from the group comprising aromatic vinyl compounds, vinyl cyanides
  • (Co)polymers which are particularly suitable are those of (a) in an amount of from 50 to 99, preferably 60 to 80 parts by weight of aromatic vinyl compounds and/or aromatic vinyl compounds which comprise substituted nuclei, such as styrene, alpha-methylstyrene, p-methylstyrene, p-chlorostyrene and/or methacrylic acid (Q - C- -alkyl esters, such as methyl methacrylate or ethyl methacrylate, and (b) in an amount of from 1 to 50, preferably 20 to 40 parts by weight vinyl cyanides (unsaturated nitrites) such as acrylonitrile and methacrylonitrile and/or (meth)acrylic acid (Q - Cg) esters (such as methyl methacrylate, n- butyl acrylate or t-butyl acrylate) and/or unsaturated carboxylic acids (such as maleic acid) and/or derivatives (such as
  • the copolymer of (a) styrene and (b) acrylonitrile (SAN) is particularly preferred.
  • (Co)polymers are thermoplastic and free from rubber.
  • the (co)polymers are known and can be produced by radical polymerization, particularly by emulsion, suspension, solution or bulk (mass) polymerization.
  • the (co)polymers preferably have molecular weights M w (weight average, as determined by GPC using laser scattering techniques and narrow molecular weight polystyrene standards) between 15,000 and 200,000.
  • (Co)polymers according to the present invention are frequently produced as byproducts during the graft polymerization of component (ii), particularly when large amounts of monomers (ii.a.l) and (ii.a.2) comprising grafting copolymer (ii.a) are grafted on to small amounts of rubber (ii.b).
  • the amount of (co)polymer which can also optionally be used according to the invention does not include these by-products of the graft polymerization of (ii). If a (co)polymer is present in the ignition resistant carbonate polymer compositions according to the invention, the ratio by weight of components (ii):(co)polymer may desirably be between 2:1 and 1:4, preferably between 1:1 and 1:2.
  • thermoplastic vinyl (co)polymer is present in an amount equal to or greater than about 0.5 parts by weight, preferably equal to or greater than about 1 part by weight, more preferably equal to or greater than about 2 parts by weight, more preferably equal to or greater than about 5 parts by weight, and more preferably equal to or greater than about 10 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • thermoplastic vinyl (co)polymer is present in an amount equal to or less than about 45 parts by weight, preferably equal to or less than about 40 parts by weight, more preferably equal to or less than about 35 parts by weight, more preferably equal to or less than about 30 parts by weight, and more preferably equal to or less than about 25 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • the ratio by weight of components (ii):(iii) may desirably be between 2:1 and 1:4, preferably between 1:1 and 1:2.
  • the ignition resistant carbonate polymer compositions of the present invention may further comprise a filler and/or reinforcing material.
  • Preferred fillers which may also have a reinforcing action, are glass fibers, carbon fibers, metal fibers, metal coated fibers, thermoset fibers, glass beads, mica, silicates, quartz, talc, titanium dioxide, and/or wollastonite alone or in combinations.
  • the filler and/or reinforcing material is present in an amount equal to or greater than about 0.5 parts by weight, preferably equal to or greater than about 1 part by weight, more preferably equal to or greater than about 2 parts by weight, more preferably equal to or greater than about 5 parts by weight, and more preferably equal to or greater than about 10 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • the filler and/or reinforcing material is present in an amount equal to or less than about 60 parts by weight, preferably equal to or less than about 40 parts by weight, more preferably equal to or less than about 30 parts by weight, more preferably equal to or less than about 25 parts by weight, and more preferably equal to or less than about 20 parts by weight based on the weight of the ignition resistant carbonate polymer composition.
  • the ignition resistant carbonate polymer composition of the present invention may further comprise an impact modifier, for example see USP 6,545,089 and US Publication 2007/0225441 which are incorporated herein by reference.
  • Preferable impact modifiers are rubber materials having a T g equal to or less than 0°C, preferably equal to or less than -10°C, more preferably equal to or less than -20°C, and most preferably equal to or less than -30°C.
  • Suitable rubbers include polymers such as styrene and butadiene (SB) copolymer, acrylate rubbers, particularly homopolymers and copolymers of alkyl acrylates having from 4 to 6 carbons in the alkyl group or polyolefin elastomers, particularly copolymers of ethylene, propylene and optionally a nonconjugated diene.
  • SB styrene and butadiene
  • acrylate rubbers particularly homopolymers and copolymers of alkyl acrylates having from 4 to 6 carbons in the alkyl group or polyolefin elastomers, particularly copolymers of ethylene, propylene and optionally a nonconjugated
  • the impact modifier is a grafted homopolymer or copolymer of butadiene that is grafted with a polymer of styrene and methyl methacrylate.
  • a grafted homopolymer or copolymer of butadiene that is grafted with a polymer of styrene and methyl methacrylate.
  • Some of the preferred rubber-containing materials of this type are the known methyl methacrylate, butadiene, and styrene (MBS) core/shell grafted copolymers having a T g equal to or less than 0°C and a rubber content greater than 40 percent, typically greater than 50 percent. They are generally obtained by graft polymerizing styrene and methyl methacrylate and or equivalent monomers in the presence of a conjugated diene polymer rubber core, preferably a butadiene homo- or co-polymer.
  • the grafting monomers may be added to the reaction mixture simultaneously or in sequence, and, when added in sequence, layers, shells or wart- like appendages can be built up around the substrate latex, or core.
  • the monomers can be added in various ratios to each other.
  • the impact modifier is a silicon-based rubber.
  • Silicon- based rubbers are well known in prior art, see US Patent Application Nos. 2007/0155857 and 2008/0090961, both of which are incorporated herein by reference.
  • a particularly suitable silicon-based rubber is an emulsion polymerized core-shell rubber having in its core a combination of silicone and acrylate.
  • Such silicon-based rubbers may be grafted by a wide variety of monomers such as styrene, acrylonitrile, methylmethacrylate,
  • Desirable silicon-based rubbers are grafted with (meth)acrylates and have a high silicone ratio in their core above, preferably the silicon content is equal to ⁇ or greater than above 10 weight percent, more preferably equal to or greater than 20 weight percent.
  • Suitable silicon-based core-shell graft copolymer prepared by graft polymerization of a vinyl monomer onto a rubber containing about 20 to about 95 percent by weight of silicon.
  • Methods for preparing a graft copolymer in the form of a silicon-based core-shell are well-known in the art and will be readily understood by a person skilled in the art.
  • the graft copolymer suitable for the present invention can have a structure in which a vinyl monomer is grafted onto a core part of the rubber, thus forming a rigid shell.
  • the kind of the silicon-based core-shell copolymer used in the invention and it may be prepared by conventional methods well-known in the art.
  • the silicon-based core-shell copolymer may be prepared by polymerizing a silicon-based rubber and then grafting one or more compounds selected from the group consisting of styrene, alpha-methylstyrene, halogen or alkyl substituted styrene, acrylonitrile, methacrylonitrile, Cj-Ce methacrylic acid alkylester, Q-Cg acrylic acid alkylester, maleic anhydride, C1-C4 alkyl and phenyl N-substituted maleimide onto the rubber.
  • styrene alpha-methylstyrene
  • halogen or alkyl substituted styrene acrylonitrile
  • methacrylonitrile methacrylonitrile
  • Cj-Ce methacrylic acid alkylester Cj-Ce methacrylic acid alkylester
  • Q-Cg acrylic acid alkylester maleic anhydride
  • the Ci-Cg methacrylic acid alkylester and CpCg acrylic acid alkylester belong to esters of methacrylic acid and acrylic acid, respectively, which are esters derived from monohydril alcohol having 1 to 8 carbon atoms. Particular examples thereof may include methacrylic acid methylester, methacrylic acid ethylester and methacrylic acid propylester.
  • the rubber content of the silicon-based core-shell graft copolymer can be in the range of about 30 to about 90 percent by weight If the rubber content is lower than about 30 percent by weight, the flame retardance of the composition can deteriorate. Meanwhile, if the rubber content exceeds about 90 percent by weight, the impact resistance of the composition can decline.
  • the silicon-based rubber core may be made of cyclosiloxane, examples of which may include hexamethylcyclotrisiloxane, octamethylcyclotetrasiloxane,
  • the silicon-based rubber may be prepared by mixing the siloxane with one or more curing agents.
  • suitable curing agents may include trimethoxymethylsilane, triethoxyphenylsilane, tetramethoxysilane, tetraethoxysilane, and the like, and mixtures thereof.
  • the silicon content of the rubber part which constitutes a core part of the composition in the present invention, can be in the range of about 20 to about 95 percent by weight. If the silicon content of the rubber part is lower than about 20 percent by weight, the flame retardance of the composition can be hindered, which can make it difficult to acquire levels of flame retardance required for products. Further, if the silicon content is greater than about 95 percent by weight, the impact resistance of the composition can be hampered, which may make it difficult to obtain impact strength required for products.
  • the silicon content to a total silicon-based core-shell graft copolymer may be in the range of about 6 to about 85.5 percent by weight.
  • the silicon content to a total silicon-based core-shell graft copolymer may be in the range of about 50 to about 85 percent by weight in terms of flame retardance and impact strength.
  • a silicon-based core-shell graft copolymer if used, it is used in an amount of equal to or greater than 0.5 parts by weight, preferably equal to or greater than 1 part by weight, and more preferable equal to or greater than 2 parts by weight based on the weight of the ignition resistant carbonate polymer composition. If the content of the silicon-based core-shell graft copolymer is lower than about 0.5 parts by weight, its effect on impact strength may be insignificant.
  • a silicon-based core-shell graft copolymer is used, it is used in an amount of equal to or greater less than 20 parts by weight, preferably equal to or less than 15 parts by weight, more preferably equal to or less than 10 parts, and more preferable equal to or less than 5 parts by weight based on the weight of the ignition resistant carbonate polymer composition. If the content thereof is greater than about 20 parts by weight, mechanical strength such as tensile strength, flexural modulus and the like may be lowered.
  • impact modifiers useful in the compositions of this invention are those based generally on a long-chain, hydrocarbon backbone, which may be prepared predominantly from various mono- or dialkenyl monomers and may be grafted with one or more styrenic monomers.
  • Representative examples of a few olefinic elastomers which illustrate the variation in the known substances which would suffice for such purpose are as follows: butyl rubber; chlorinated polyethylene rubber (CPE); chlorosulfonated polyethylene rubber; an olefin polymer or copolymer such as ethylene/propylene (EP) copolymer,
  • ES ethylene/styrene
  • EPDM ethylene/propylene/ diene
  • the impact modifier is preferably present in an amount of at least about 1 part by weight, preferably at least about 2 parts by weight, more preferably at least about 5 parts by weight, even more preferably at least about 7.5 parts by weight, and most preferably at least about 10 parts by weight based on the total weight of the polymer blend composition.
  • the impact modifier is present in an amount less than or equal to about 30 parts by weight, preferably less than or equal to about 25 parts by weight, more preferably less than or equal to about 20 parts by weight, even more preferably less than or equal to about 15 parts by weight, and most preferably less than or equal to about 10 parts by weight based on the weight of the polymer blend composition.
  • the ignition resistant carbonate polymer compositions comprising components (i),
  • (ii), (iii), (iv), (v) and (vi) are produced by mixing the particular components in a known manner and melt-compounding and/or melt-extruding them at temperatures of from 200°C to 300°C in conventional units such as internal kneaders, extruders and twin-screw extruders.
  • the individual components may be mixed in a known manner both in succession and simultaneously and both at approximately 23°C (room temperature) and at a higher temperature.
  • the present invention accordingly also provides a process for the production of the ignition resistant carbonate polymer compositions.
  • the ignition resistant carbonate polymer compositions according to the invention are suitable for the production of fabricated articles of any kind, in particular those subject to stringent requirements with regard to mechanical properties and especially requiring good flow properties.
  • the ignition resistant carbonate polymer compositions of the present invention are thermoplastic. When softened or melted by the application of heat, the ignition resistant carbonate polymer compositions of this invention can be formed or molded into fabricated articles using conventional techniques such as compression molding, injection molding, gas assisted injection molding, calendaring, vacuum forming, thermoforming, extrusion and/or blow molding, alone or in combination.
  • the ignition resistant polymer compositions can also be fabricated, formed, spun, or drawn into films, fibers, multi-layer laminates or extruded into sheets and/or profiles.
  • fabricated articles which may be produced are: enclosures of all kinds, for example for domestic appliances such as juice extractors, coffee machines, food mixers, for office equipment, such as monitors, printers, copiers or cladding sheet for the building sector and automotive components. They may also be used in electrical engineering applications as they have very good electrical properties.
  • the ignition resistant carbonate polymer compositions according to the invention may furthermore, for example, be used to produce the following fabricated articles or shaped articles: interior trim for rail vehicles, interior and exterior automotive applications, enclosures for electrical devices containing small transformers, enclosures for information dissemination and transmission devices, enclosures and cladding for medical purposes, massage devices and enclosures therefore, toy vehicles for children, sheet wall elements, enclosures for safety equipment, hatchback spoilers, thermally insulated transport containers, apparatus for keeping or caring for small animals, articles for sanitary and bathroom installations, cover grilles for ventilation openings, articles for summer houses and sheds, and enclosures for garden appliances.
  • Preferred fabricated articles include housings or enclosures such as for: power tools, appliances, consumer electronic equipment such as TVs, VCRs, DVD players, web appliances, electronic books, etc., or housings or enclosures such as for: information technology equipment such as telephones, computers, monitors, fax machines, battery chargers, scanners, copiers, printers, hand held computers, flat screen displays, etc.
  • the present invention accordingly also provides the use of the ignition resistant carbonate polymer compositions according to the invention for the production of fabricated articles of all kinds, preferably those stated above, and the articles made from the ignition resistant carbonate polymer compositions according to the invention.
  • compositions of Examples 1 to 7 and Comparative Examples A to Dare melt compounded in a Werner and Pfleiderer ZSK-25 25 mm twin-screw co-rotating extruder The temperature profile from the hopper to the nozzle is 220°C to 265°C. Prior to compounding, the polycarbonate is dried for at least 4 hours at 120°C.
  • a four feeder system is used: a mixture of polycarbonate and ABS pellets is fed via one feeder, powdered additives are added as a dry blend via a second feeder, the BAPP is added at 80°C via a liquid feeder, and the PET is added via a fourth feeder.
  • the mold release agent is sprayed onto the polycarbonate pellets prior to feeding them into the extruder.
  • the throughput is 10 kilograms per hour; the extrudate is cooled in a 50°C water bath and commuted to pellets.
  • Mechanical and thermal property test specimens measuring 3.2mm thick are injection molded on a Demag IntElect 80/370-310 type electrical injection molding machine with the following parameters: Barrel Profile, nozzle to hopper: 290°C to 250°C ; Mold Temperature: 80°C; and Cycle Time: 57 seconds.
  • IntElect 80/370-310 type electrical injection molding machine with the following parameters: Barrel Profile, nozzle to hopper: 235°C to 240"C ; Mold Temperature: 60°C; and Cycle Time: 39.5 seconds.
  • UL 94 burn test specimens measuring 2.5mm thick are injection molded on a Demag IntElect 80/370-310 type electrical injection molding machine with the following parameters: Barrel Profile, nozzle to hopper: 235°C to 240°C ; Mold Temperature: 60°C; and Cycle Time: 42 seconds.
  • PC is a bisphenol-A polycarbonate homopolymer having a melt flow of 23 and commercially available as CALIBRETM 300-23 from the Dow Chemical Company.
  • mABS is a mass polymerized acrylonitrile, butadiene, and styrene terpolymer having about 20 percent acrylonitrile, 15 percent butadiene rubber, and an average rubber particle size (Dv) as determined by Coulter Counter of 1.15 microns;
  • eABS is an emulsion polymerized acrylonitrile, butadiene, and styrene terpolymer having about 12 percent acrylonitrile and 48 percent butadiene rubber;
  • SAN is a styrene and acrylonitrile copolymer comprising 75 percent styrene and 25 acrylonitrile having a melt flow rate of 4.5 (determined at 230°C under a load of 3.8kg);
  • PET-1 is a semi-crystalline polyethylene terephthalate with an intrinsic viscosity of 0.64 dl/g available as PET LIGHTERTM C73 from Equipolymer;
  • PET-2 is a semi-crystalline polyethylene terephthalate with an intrinsic viscosity of 0.80 dl g available as PET LIGHTER C93 from Equipolymer;
  • ' ⁇ ' is an oligomeric phosphate flame retardant comprising bisphenol-A bis(diphenyl phosphate) having an average 'n' value of about 1.13 available as REOFOSTM BAPP from Chemtura Corporation;
  • PTFE-1 is an anti-drip agent comprising a mixture if a fibril forming
  • PTFE-2 is an anti-drip agent comprising a fibril forming polytetrafluoroethylene having an average particle size of 550 microns, a bulk density of 500 g 1, a specific gravity of 2.17, and a Rheometric Pressure of 8 MPa according to ASTM D4895 available as ALGOFLONTM DF210 from Solvay;
  • MRA is a liquid mold release agent comprising octyldodecyl stearate available as LOXIOLTM 3820 from Cognis;
  • ANTIOX is a phenolic antioxidant available as IRGANOXTM 1076 from Ciba
  • UL-94 is The Underwriters Laboratories' Standard 94 flammability test which is performed on 1.5 millimeter (mm) and 2.5mm test specimens. Ratings are according to the standard;
  • HDT heat deflection temperature determined at 1.80 MPa according to ISO 75A using a Ceast heat deflection temperature apparatus
  • Vicat softening temperature is determined on a Ceast HDT 300 Vicat machine in accordance with ISO 306 at 120° per hour and 1 kg;
  • mm 24 "Izod" impact resistance as measured by the Notched Izod test is determined according to ISO 180/lA at 23°C. Test specimens measured 10 mm x 80 mm x 4 mm. The specimens were notched with a notcher to give a 250 micrometer radius notch. A Zwick 5110 Izod impact testing unit was used; and
  • Modulus property testing is done in accordance with ISO 527 at room temperature using an Zwick 1455 mechanical tester, tensile strength and elongation are performed at a rate of 50 mm min and tensile modulus is performed at a rate of lmm/min.
  • the examples of the invention comprising the low viscosity semi-crystalline polyester and a mass polymerized graft copolymer demonstrate a better combination of flammability, physical, thermal, and flow length performance as compared to the comparative examples comprising the high viscosity polyester and/or emulsion polymerized graft copolymer.

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Abstract

La présente invention porte sur une composition de polymère de carbonate ignifuge, sur un procédé pour fabriquer ladite composition et sur des articles fabriqués formés à partir de celle-ci. La composition de polymère de carbonate ignifuge est constituée de : (i) un polycarbonate aromatique ou un polyestercarbonate aromatique, (ii) un (co)polymère greffé produit par polymérisation en masse, (iii) un polymère poly(dicarboxylate d'alkylène) semi-cristallin thermoplastique ayant une viscosité intrinsèque de 0,4 à 0,7 dl/g, (iv) un composé phosphate aromatique représenté par la formule (I) : dans laquelle, R1, R2, R3 et R4 représentent chacun indépendamment des autres un alkyle en C1 à C8 éventuellement halogéné ou cycloalkyle en C5 à C6, aryle en C6 à C20 ou aralkyle en C7 à C12, dans chaque cas éventuellement substitué par un alkyle et/ou halogène, X désigne un radical aromatique mononucléaire ou polynucléaire ayant 6 à 30 atomes de C, chaque n représente indépendamment des autres 0 ou 1 et N représente des valeurs de 0 à 30, (v) un polymère polytétrafluoroéthylène, un thermoplastique fluoré, ou un mélange de ceux-ci, et (vi) un ou plusieurs composants parmi un (co)polymère vinylique thermoplastique, un modificateur de la résistance au choc, une charge, un matériau de renforcement, un stabilisant, un pigment, un colorant, un agent de démoulage, un lubrifiant ou un agent antistatique.
EP11706760A 2010-03-02 2011-03-02 Composition de polymère de carbonate ignifuge à écoulement amélioré Ceased EP2542622A1 (fr)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11339263B2 (en) 2015-03-16 2022-05-24 Shpp Global Technologies B.V. Fibrillated polymer compositions and methods of their manufacture

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105612202B (zh) * 2013-10-08 2019-10-11 科思创德国股份有限公司 纤维复合材料、其用途及其制备方法
EP3116971B1 (fr) * 2014-03-14 2018-06-06 Covestro Deutschland AG Compositions thermoplastiques thermiquement conductrices à transformabilité équilibrée
US10639870B2 (en) 2014-11-17 2020-05-05 Hewlett-Packard Development Company, L.P. Polymer fiber composite
WO2017175788A1 (fr) * 2016-04-06 2017-10-12 株式会社カネカ Composition de résine de polycarbonate, et article moulé associé
EP3293222A1 (fr) 2016-09-09 2018-03-14 Trinseo Europe GmbH Article composite multicouches comprenant une couche polyurethane et une couche pc/abs
CN111417445B (zh) * 2017-12-01 2022-05-17 乐高公司 由pet聚合物材料制成的玩具搭建元件
CN109306187B (zh) * 2018-08-23 2021-02-05 苏州普科环境技术有限公司 一种新能源汽车用高阻燃复合材料及其制备方法
EP3786226A1 (fr) 2019-08-27 2021-03-03 Trinseo Europe GmbH Compositions stabilisées de polycarbonates et de composés aromatiques substitués par du vinylidène
TWI810751B (zh) * 2021-12-21 2023-08-01 南亞塑膠工業股份有限公司 耐衝擊的聚酯組成物及其製品

Family Cites Families (39)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2465319A (en) 1941-07-29 1949-03-22 Du Pont Polymeric linear terephthalic esters
US2822348A (en) 1951-11-14 1958-02-04 Du Pont Ester interchange catalysts
US2727881A (en) 1952-10-03 1955-12-20 Eastman Kodak Co Organo-titanium catalysts for the preparation of polyesters
US2720502A (en) 1952-10-03 1955-10-11 Eastman Kodak Co Organo-metallic titanium catalysts for the preparation of polyesters
NL104015C (fr) 1953-10-16
IT595468A (fr) 1957-08-22
US3047539A (en) 1958-11-28 1962-07-31 Goodyear Tire & Rubber Production of polyesters
US3243481A (en) 1962-01-08 1966-03-29 Dow Chemical Co Process for making graft copolymers of vinyl aromatic compounds and stereospecific rubbers
US3419634A (en) 1966-01-03 1968-12-31 Gen Electric Organopolysiloxane polycarbonate block copolymers
FR1580834A (fr) 1968-01-04 1969-09-12
US3660535A (en) 1970-09-23 1972-05-02 Dow Chemical Co Process for the production of alkenyl aromatic polymers containing a reinforcing polymer therein
US4156069A (en) 1976-04-02 1979-05-22 Allied Chemical Corporation Bisphenol-A/terephthalate/carbonate melt processable copolymers
US4260731A (en) 1978-09-11 1981-04-07 Mitsubishi Chemical Industries, Ltd. Aromatic polyester-polycarbonate
US4239863A (en) 1979-06-28 1980-12-16 The Dow Chemical Company Process for the polymerization of acrylonitrile-butadiene-styrene resins
US4529791A (en) 1981-01-28 1985-07-16 The Dow Chemical Company Interfacial polycarbonate preparation by adding additional solvent
US4558141A (en) 1981-11-19 1985-12-10 E. I. Du Pont De Nemours And Company Perfluorodioxole and its polymers
US4401804A (en) 1982-05-24 1983-08-30 Eastman Kodak Company Deactivation of polyester catalyst residues
US4677162A (en) 1983-04-15 1987-06-30 Mobay Corporation Polycarbonate blends having low gloss
US4532290A (en) 1984-05-02 1985-07-30 General Electric Company Stabilized polycarbonate-polyester compositions
DE3738143A1 (de) 1987-11-10 1989-05-18 Bayer Ag Verwendung von redoxpfropfpolymerisaten zur verbesserung der benzinbestaendigkeit von thermoplastischen, aromatischen polycarbonat- und/oder polyestercarbonat-formmassen
DE3819081A1 (de) 1988-06-04 1989-12-07 Bayer Ag Flammwidrige, schlagzaehe polycarbonat-formmassen
NL8802346A (nl) 1988-09-22 1990-04-17 Gen Electric Polymeermengsel met aromatisch polycarbonaat, styreen bevattend copolymeer en/of entpolymeer en een vlamvertragend middel, daaruit gevormde voorwerpen.
USRE36188E (en) 1989-09-20 1999-04-06 General Electric Company Polymer mixture having aromatic polycarbonate styrene I containing copolymer and/or graft polymer and a flame-retardant, articles formed therefrom
US5922816A (en) 1992-06-02 1999-07-13 General Electric Company Polyester-polycarbonate compositions stabilized against ester-carbonate interchange
DE4328656A1 (de) 1993-08-26 1995-03-02 Bayer Ag Flammwidrige, spannungsrißbeständige Polycarbonat-ABS-Formmassen
US5714262A (en) 1995-12-22 1998-02-03 E. I. Du Pont De Nemours And Company Production of poly(ethylene terephthalate)
DE19734659A1 (de) 1997-08-11 1999-02-18 Bayer Ag Flammwidrige Polycarbonat-ABS-Formmassen
US6545089B1 (en) 1997-09-04 2003-04-08 General Electric Company Impact modified carbonnate polymer composition having improved resistance to degradation and improved thermal stability
DE19853105A1 (de) 1998-11-18 2000-05-25 Bayer Ag Flammwidrige Polycarbonat-ABS-Formmassen
DE19914139A1 (de) 1999-03-27 2000-09-28 Bayer Ag Flammwidrige, schlagzähmodifizierte Polycarbonat-Formmassen
US6380304B1 (en) 1999-09-30 2002-04-30 The Dow Chemical Company Mass polymerized rubber-modified monovinylidene aromatic copolymer compositions
WO2001027197A1 (fr) 1999-10-14 2001-04-19 Dyneon Llc Additif de traitement pour polymeres pouvant etre travailles a l'etat de fusion
US7446144B2 (en) * 2005-09-14 2008-11-04 Bayer Materialscience Llc Thermoplastic molding composition and articles thermoformed therefrom
KR100838451B1 (ko) 2005-12-30 2008-06-16 제일모직주식회사 내열도가 높고, 내충격성이 우수한 난연성 폴리카보네이트수지 조성물
DE102006012988A1 (de) 2006-03-22 2007-09-27 Bayer Materialscience Ag Flammgeschützte schlagzähmodifizierte Polycarbonat-Zusammensetzungen
CN101104731A (zh) * 2006-07-14 2008-01-16 上海普利特复合材料有限公司 一种无卤阻燃聚碳酸酯/热塑性聚酯树脂组合物
US9127154B2 (en) 2006-10-13 2015-09-08 Bayer Materialscience Llc Impact resistant, flame retardant thermoplastic molding composition
KR100804173B1 (ko) 2006-11-23 2008-02-18 제일모직주식회사 난연성 열가소성 수지 조성물
ES2459500T3 (es) * 2008-08-06 2014-05-09 Styron Europe Gmbh Composición de polímero de carbonato resistente a la ignición

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2011107273A1 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11339263B2 (en) 2015-03-16 2022-05-24 Shpp Global Technologies B.V. Fibrillated polymer compositions and methods of their manufacture

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