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    • 专利摘要:
    The invention relates to flame-retardant, expandable polymers. According to the invention, it is provided that melaminium thiosulphate (bis (2,4,6-triamine-1,3,5-triazinium) thiosulphate) is contained as a flame retardant synergist as a constituent of a flame retardant composition or in combination with at least one flame retardant.
    公开号:AT511090A4
    申请号:T545/2011
    申请日:2011-04-18
    公开日:2012-09-15
    发明作者:
    申请人:Sunpor Kunststoff Gmbh；
    IPC主号:
    专利说明:

    Flame-retardant expandable polymers
    The present invention relates to flame-retardant, at least one blowing agent-containing, expandable polymers.
    The invention further relates to a process for the preparation of these polymers, further with this flame retardants protected polymer foams and processes for their preparation, and the particular use of the above flame retardants in expandable polymers and polymer foams.
    STATE OF THE ART
    The equipment of polymer foams with flame retardants is important for many areas. The regulations governing the use of expandable polystyrene (EPS) or expanded polystyrene (XPS) expanded polystyrene foam as building insulation generally require flame retardant equipment. Polystyrene homopolymers and copolymers are made flame retardant with halogenated, in particular brominated organic compounds such as hexabromocyclododecane (HBCD). However, these and a number of other brominated substances have come into discussion or have already been banned because of their potential environmental and health hazards.
    As an alternative, there are many halogen-free flame retardants. However, halogen-free flame retardants generally have to be used in significantly higher amounts in order to achieve the same flameproofing effect of the halogen-containing flame retardants.
    Partly for this reason, halogen-free flame retardants, which are replaceable in compact thermoplastic polymers, often can not be used in the same way in polymer foams, since they either interfere with the foaming process or influence the mechanical and thermal properties of the polymer foam. In the production of expandable polystyrene by suspension polymerization, the high flame retardant can also reduce the stability of the suspension and thus interfere with the production process or affect.
    The effect of the flame retardants used in compact polymers in polymer foams is often unpredictable due to the peculiarities of such foams and the different fire behavior or because of different fire tests.
    Various phosphorus-based flame retardants are known in the art. In this regard, WO 2006/027241 describes a halogen-free flame retardant for polymer foams based on 9: 10-dihydro-9-oxa-10-phospha-phenanthrene-10-oxide (6H-dibenz [c, e] -oxaphosphorine-6-oxide, DOPO , CAS [35948-25-5]) and its derivatives. This flame retardant is replaceable, but high concentrations must be added and at the same time DOPO has a strong softening effect, so that with sufficient flame retardancy required in most European countries for construction products requirements for mechanical stability, is no longer achievable.
    US 5,811,470 discloses a flame retardant system consisting of an organic halogen-free phosphorus compound and elemental sulfur in styrenic polymers. Polymer foams, in particular polystyrene foams are not considered. The use of elemental sulfur has the disadvantage that in the production of expandable polymers, their processing and in the final product, the resulting in side reactions of organic sulfur compounds represent an intense odor.
    In AT 508.304 or AT 508.507, flame retardant systems are described in polymer foams, with DOPO or DOPS as flame retardant and with sulfur and / or at least one sulfur-containing compound or sulfur compound as flame retardant synergist. Such polymer foams meet the minimum requirements for foamability and mechanical stability. However, an unpleasant side-effect, especially of sulfur, as well as many sulfur compounds, is that odorous compounds may form during processing.
    Object of the present invention is thus to provide a good fire-resistant, flame-retardant, expandable polymer with low content of flame retardants and good quality, especially good foamability and good mechanical stability, and especially with non-irritating odor properties.
    Furthermore, it is an object of the invention to provide an advantageous process for the preparation of such polymers.
    A further object of the invention is to provide a halogen-free flame-retardant, but qualitatively corresponding, polymer foam with advantageous fire behavior, non-irritating odor properties as well as good mechanical properties and an advantageous production method therefor.
    It is particularly desirable that the polymer or polymer foam also meet the stringent fire resistance requirements for e.g.
    Construction applications met, such as the B2 small burner test according to DIN 4102-2 or the small burner test according to EN 11925-2.
    DISCLOSURE OF THE INVENTION
    This object is achieved for the polymer of the type mentioned by the characterizing features of claim 1. According to the invention, it is provided that melaminium thiosulphate (bis (2,4,1,6-triamine-1,3,5-triazinium) thiosulphate)
    NIL NH, N- / 7
    NH2- < . NH Θ eo-s-θ © NH NH N NH, N-0
    'F ^ N NH. NH,
    Melaminium thiosulfate (MelTS) is contained as Flammschutzsynergist as part of a flame retardant composition or in combination with at least one flame retardant. Surprisingly, it has been found that melamine (ium) thiosulphate, which in itself does not exhibit any flameproofing effect even in relatively high concentrations, in combination with a flame retardant, for example with phosphorus compounds, produces a surprisingly good increase in the flame retardant effect.
    Through the use of melamine thiosulphate, the total amount of flame retardant can be reduced, resulting in a variety of benefits, i.a. in the production process, in the cost, the mechanical properties of the product, etc., leads. Above all, the foaming process and the mechanical properties of the foam are not appreciably affected, resulting in a high quality product.
    Also surprising is the extremely low odor activity of the synergist melamine thiosulfate.
    Advantageous developments of these polymers are described by the features of the dependent claims:
    Thus, it is advantageously provided that melaminium thiosulfate in an amount of 1 to 25 wt.%, In particular in an amount of 2 to 15 wt%, based on the total weight of the polymer or of the granules thus obtained is included.
    Furthermore, it is already advantageous for environmental reasons, if only halogen-free flame retardants are included,
    In this context, it is advantageous in terms of fire behavior, if at least one phosphorus compound is contained as a flame retardant, wherein the phosphorus compound is selected from elemental phosphorus, in particular red phosphorus, and / or at least one inorganic phosphorus compound or hydrolysates or salts thereof and / or at least an organic phosphorus compound represented by the following general formula (I) or (II) or hydroxysates or salts thereof: RrP = 0 r ~ p: tt'r3 (0 (II) wherein R1t R2 and R3 are each independently of one another organic or inorganic Mean residues.
    In the present text, the term phosphorus compounds is understood to mean or subsume elemental phosphorus as well as organic and inorganic phosphorus compounds and / or phosphorus-containing compounds and hydroxysates or salts thereof. Elemental phosphorus occurs in four allotropic modifications as white, red, black and purple phosphorus. Each of these basic types forms different crystal structures, which also results in differences in physical properties and reactivities. As a flame retardant, the red phosphorus is most advantageously used. As inorganic phosphorus compounds are advantageously the (poly) phosphates, such as non-condensed salts of phosphorous acid or condensed salts, such as ammonium phosphate and ammonium polyphosphate in question.
    The substituents or radicals R1 R2 and R3 of the organic phosphorus compound are independent of each other and may be the same or different or even completely absent. The radicals R may each, independently of one another, preferably denote -H, substituted or unsubstituted C 1 -C 20 -alkyl, C 1 -C -alkenyl, C 3 -C 8 -cycloalkyl, C 6 -C 18 -aryl, C 7 -C 30 -alkylaryl, (VCe Alkoxy or (VCe-alkylthio, or -OH or -SH and alkali metal, alkaline earth metal, ammonium or phosphonium salts thereof.
    By the " alkyl " portion of the optional substituents R of the phosphorus compounds of formula (II) is meant both saturated and unsaturated aliphatic, which may be straight or branched, with unsaturated groups being preferred. The substituents R preferably include short chain alkyl groups of not more than 6, more preferably not more than 4 or 3, even more preferably not more than 2, carbon atoms or phenyl as the aryl group. Shorter chain residues are preferred because longer chain residues, a high degree of saturation, and a greater number of substituents can adversely affect the flame retardancy. Particularly effective phosphorus compounds are preferably unsubstituted as possible.
    If substituents R are present, these preferably have a sulfur-containing substituent, such as e.g. -SH, -SO3NH4 -SO- or -SO 2 -, or a phosphorus-containing substituent, such as. -PO (ONH4) 2 or the like, so as to further improve the flame retardancy.
    Of the optional salts of any SH or OH groups of the phosphorus compounds, ammonium and phosphonium salts are preferred, as these may also contribute to the flame retardancy. The ammonium and phosphonium ions can instead of hydrogen atoms in each case up to four organic radicals, for. Substituents R as defined above (i.e., NR4 + and PR4 +, respectively), but in the case of ammonium hydrogen is preferred as the substituent.
    Examples of such phosphorus compounds of the general formula (II) or (III) are organic phosphorus compounds and salts thereof, such as the monomeric organic phosphorus compounds, including phosphoric acid ester, phosphoric acid amide ester and phosphonitrile compounds, organic phosphorous acid compounds, such as phosphorous acid esters, compounds the hypophosphorous acid, the phosphines and phosphine oxides such as triphenylphosphine, triphenylphosphine oxide and tricresylphosphine oxide, etc.
    In particular, it has proven useful if the flame retardant is an organic phosphorus compound, namely a 9,10-dihydro-9-oxa-10-phosphaphenanthren derivative of the general formula (III) or (IIIa) or a salt or ring-opened hydrolyzate thereof
    (NI) (IIIa) wherein: X is in particular: substituted or unsubstituted C 1 -C 4 -alkyl, C 1 -C 15 -alkenyl, C 3 -C 8 -cycloalkyl, C 6 -C 18 -aryloxy, C 7 -C 30 -alkylaryl, C 6 -C 10 -alkoxy or C 1 -C 8 Alkylthio, or alkali metal, alkaline earth metal, ammonium or phosphonium salts thereof, and X is in particular selected from -H, -OH, -SH, -ONH4, -SNH (Et) 3, -ONH (Et) 3, omega-amine, guanidine; Y, Y2 and Z each independently represent an oxygen atom or a sulfur atom; n is an integer of at least 1, wherein when Z is an oxygen atom, n = 1, and when Z is a sulfur atom, n = 1 to 8; each of the optional R m groups independently represents an alkyl, alkoxy or alkylthio group having 1 to 8 carbon atoms or an aryl group, and each m is independently an integer of 0 to 4.
    Furthermore, it is advantageous if at least one of the following phosphorus compounds is present as flame retardant: - Phosphorus compound according to formula (Ia):
    (la) 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO-OH) - or salts thereof according to formula (Ib):
    (Ib) (DOPO-OR) - or their ring-opened hydrolysates according to formula (Ic): ♦ · • · · «· · / / / / / / & · ···» »» »» »» »» »» »» »» »» »» »» »» »» »» »» »» »· · · · · · · · · · · · gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß gemäß. • »« * · · ί! &Quot; " ΐί Ο 'Ρ- ΟθΘρ ΟΗ ΟΗ (lc).
    With these phosphorus compounds, it is possible to achieve high-quality, highly fire-resistant polymers meeting the standards even at low levels of flame retardants. The polymers have good foamability, good mechanical stability and no disturbing odor properties.
    In this case, it is possible, for example, that the radical R® is an organic or inorganic cation, in particular a salt of a quaternary ammonium compound NR / or a quaternary phosphonium compound PR /, since these can also contribute to the flame retardancy. The ammonium and phosphonium compounds may each have up to four organic radicals (i.e., NR4® and PR4®, respectively) instead of hydrogen atoms.
    In this context, it has been found to be particularly advantageous if the radical R® in the general formula (Ib) or (lc) NH4® and thus the phosphorus compound, the 10-hydroxy-9,10-dihydro-9-oxa-10 phosphaphenanthrene 10-oxide ammonium salt is: -N.
    NH I NH, DOPO-ONH,
    Furthermore, it has been found to be particularly advantageous if the radical R® in the general formula (Ib) or (Ic) is guanidinium and thus the phosphorus compound is the 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene- 10-oxide guanidinium salt is: • · · * * Μ Μ: 8; * · · · «IX .O .0 ΝΗ, ° θ Α '/ ΝΗ. - ΝΗ- DOPO-OGua
    Furthermore, it has been found to be particularly advantageous if the radical R® in the general formula (Ib) or (Ic) is melamine and thus the phosphorus compound is the 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene- 10-oxide melamine salt is:
    .0 O o MH. NH i
    NH
    N
    NH DOPO-OMel
    These compounds have, on their own or as a mixture of several or in a flame retardant composition, very good flame retardancy. With these flame retardants polymers and polymer foams with improved flame retardancy and improved properties could be created. In addition, even comparatively lower amounts - which do not interfere with foaming - are sufficient in order to achieve the same effect. In particular, these compounds have no interfering softening properties. Surprisingly, it has been found that such flame-retardant polymers and polymer foams have an unexpectedly improved mechanical stability, e.g. with the compound DOPO. In addition, no disturbing odors occur during processing. For certain applications preferred flame retardants can be selected from the list of claim 11.
    The expandable polymers according to the invention are preferably expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS), which consist in particular of homopolymers and copolymers of styrene, preferably glass-clear polystyrene (GPPS), impact-modified polystyrene (HIPS), anionically polymerized polystyrene or Schjagstähpolystyrol (A-IPS), styrene-alpha-methylstyrene copolymers, acrylonitrile-butadiene-styrene polymers (ABS), styrene-acrylonitrile (SAN) acrylonitrile-styrene-acrylic ester (ASA), methacrylate-butadiene-styrene (MBS), methyl methacrylate-acrylonitrile-butadiene-styrene (MABS) polymers or mixtures thereof or with polyphenylene ether (PPE). Especially for polystyrene, the need for high-quality products is particularly high.
    Furthermore, this flame retardant system is suitable for thermoplastic polymers, such as cellulose acetate butyrate (CAB) or cellulose acetate butyrate-containing mixtures, as well as for expandable polymers consisting of polylactic acid (PLA) or polylactic acid (PLA).
    Said styrene polymers may be used to improve the mechanical properties or the temperature resistance, if appropriate by using compatibilizers with thermoplastic polymers such as polyamides (PA), polyolefins such as polypropylene (PP) or polyethylene (PE), polyacrylates such as polymethyl methacrylate (PMMA), polycarbonate (PC), polyesters, such as polyethylene terephthalate (PET) or polybutylene terephthalate (PBT), polyethersulfones (PES), polyether ketones or polyether sulfides (PES) or mixtures thereof, generally in proportions of not more than 30% by weight, preferably in the range of 1 to 10 wt .-%, based on the polymer melt, are mixed.
    Furthermore, mixtures in the above amounts ranges with z. B hydrophobically modified or functionalized polymers or oligomers, rubbers such as polyacrylates or polydienes, z. As styrene-butadiene block copolymers, biodegradable aliphatic or aliphatic / aromatic copolyesters or thermoplastic polymers such as cellulose acetate butyrate or thermoplastic polyurethane possible.
    Suitable compatibilizers are e.g. Maleic anhydride-modified styrene copolymers, polymers containing epoxy groups or organosilanes.
    The effectiveness of the phosphorus compounds can be further improved by the addition of further suitable flame retardant synergists, such as the thermal radical formers dicumyl peroxide, di-tert-butyl peroxide or dicumyl.
    In addition, other flame retardants, such as melamine, Melamincyanu rate, metal oxides, metal hydroxides, phosphates, phosphinates or synergists such as Sb203 or Zn compounds can be used.
    If the complete absence of halogens of the polymer or of the polymer foam can be dispensed with, halogen-reduced foams can be used by the
    Use of the phosphorus compounds and the addition of lesser amounts of halogen-containing, in particular brominated flame retardants, such as hexabromocyclododecane (HBCD), preferably in amounts ranging from 0.05 to 1, in particular 0.1 to 0.5 wt%, are produced.
    Another aspect of the invention relates to the preparation of such polymers. According to the invention, the above-mentioned flame-retardant, expandable polymers can be prepared by admixing a flame retardant and melamine thio-sulfate in a conventional manner.
    An advantageous method procedure envisages that the flame retardant and melamine thiosulphate and a blowing agent are mixed with a polymer melt, for example a styrene polymer melt, with the aid of a dynamic or static mixer and then granulated.
    Alternatively it can be provided that the flame retardant, and melamine thiosulfate are added by means of a dynamic or static mixer to the polymer and melted, and then the melt is mixed with propellant and granulated.
    Alternatively, it can further be provided that the flame retardant and melamine thiosulphate, by means of a mixer to still granular expandable polymer, for example, polystyrene (EPS) are added and then the mixture is melted and granulated.
    Alternatively, it may be further contemplated that granule production by suspension polymerization of the monomer, e.g. of styrene, in aqueous suspension in the presence of the flame retardant and melamine thiosulfate and a propellant.
    A further process according to the invention for the preparation of the flame-retardant expandable styrene polymers (EPS) according to the invention comprises the steps:
    Co-dosing into an extruder of PS or EPS granules having a molecular weight of Mw > 120 000 g / mol, preferably from 150 000 to 250 000 g / mol, more preferably from 180 000 to 220 000 g / mol, and of the flame retardant, and melamine thiosulfate and optionally one or more further additives,
    co-melting of all components in the extruder optional addition of at least one blowing agent mixture of all components at a temperature > 120X
    Granulation by means of pressurized underwater granulation, e.g. 1-20 bar, to a granule size < 5 mm, preferably 0.2 to 2.5 mm, at a water temperature of 30 to 100 ° C, in particular 50 to 80 ° C, optionally superficial coating with coating agents, e.g. Silicates, metal salts of fatty acids, fatty acid esters, fatty acid amides.
    The halogen-free flame-retardant, expandable polymers according to the invention, such as styrene polymers (EPS) and styrene polymer extrusion foams (XPS), can be prepared by mixing a blowing agent, a flame retardant and melamine thiosulphate into the polymer melt and subsequent extrusion into foam sheets, foam strands or expandable granules.
    Preferably, the expandable styrenic polymer has a molecular weight > 120,000, more preferably in the range of 180,000 to 220,000 g / mol. Due to the reduction in molecular weight by shear and / or temperature, the molecular weight of the expandable polystyrene is usually about 10,000 g / mol below the molecular weight of the polystyrene used.
    The styrene polymer melt may also be blended with polymer recyclates of said thermoplastic polymers, in particular styrene polymers and expandable styrene polymers (EPS) in amounts which do not substantially impair their properties, generally in amounts of at most 50% by weight, in particular in amounts of from 1 to 20 wt .-%.
    As a rule, one or more blowing agents in homogeneous distribution are added to the polymer melt in a proportion of 2 to 10% by weight, preferably 3 to 7% by weight, based on the polymer melt. Suitable blowing agents are the physical blowing agents commonly used in expandable polystyrene (EPS), such as aliphatic hydrocarbons having 2 to 7 carbon atoms, alcohols, ketones, ethers or halogenated hydrocarbons. Preference is given to using isobutane, n-butane, isopentane, n-pentane. For XPS, preference is given to using CO 2 or mixtures with alcohols or ketones.
    The added amount of blowing agent is chosen so that the expandable polymers, in particular styrene polymers (EPS) have an expansion capacity of 7 to 200 g / l, preferably 10 to 50 g / l.
    The expandable styrene polymer pellets (EPS) according to the invention generally have a bulk density of at most 700 g / l, preferably in the range from 590 to 660 g / l.
    Further, the styrenic polymer melt may contain additives, nucleating agents, fillers, plasticizers, soluble and insoluble inorganic and / or organic dyes and
    Pigments, e.g. IR absorbers, such as carbon black, graphite, petroleum coke, anthracite or aluminum powder, together or spatially separated, e.g. via mixers or side extruders. In general, the dyes and pigments are added in amounts ranging from 0.01 to 30, preferably in the range of 1 to 10 wt .-%, added. For the homogeneous and microdispersed distribution of the pigments in the styrene polymer, it may be expedient, in particular in the case of polar pigments, to use a dispersing aid, for example organosilanes, polymers containing epoxide groups or maleic anhydride-grafted styrene polymers. Preferred plasticizers are mineral oils, phthalates, which can be used in amounts of from 0.05 to 10% by weight, based on the styrene polymer.
    A further aspect of the invention relates to a polymer foam, in particular a styrene polymer particle foam or an extruded polystyrene rigid foam (XPS) containing melaminium thiosulfate (bis (2) 4,6-triamine-1,3,5-triazinium) thiosulfate) as flame retardant synergists Component of a flame retardant composition or, in combination with at least one known flame retardant, in particular with at least one advantageous phosphorus compounds.
    An advantageous polymer foam is obtainable from the inventive flame-retardant expandable polymers, in particular from expandable styrene polymers (EPS), in particular by foaming and sintering of the polymer beads or by extrusion of the granules.
    The halogen-free, flameproofed polymer foams preferably have a density in the range from 8 to 200 g / l, more preferably in the range from 10 to 50 g / l and are preferably more than 80%, particularly preferably 95 to 100%, closed. cell-like or have a predominantly closed-cell structure with more than 0.5 cells per mm3.
    According to the invention is melamine thiosulfate (bis (2,4,6-triamine-1,3,5-triazinium) thiosulfate) as Flammschutzsynergist as part of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the above-mentioned advantageous phosphorus compounds, in expandable polymers, in particular in expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS) or in polymer foams, in particular in styrene polymer particle foams obtainable by foaming from expandable polymers, or in extruded polystyrene rigid foams (XPS) used.
    For the production of flame-retardant extruded polystyrene rigid foam (XPS), the flame retardants, melaminium thiosulfate and a blowing agent are mixed with a styrene polymer melt by means of a dynamic or static mixer and then foamed or the phosphorus compounds and melaminium thiosulfate by means of a dynamic or static mixer to still granular polystyrene polymer mixed and melted, and then added to the melt with blowing agent and foamed.
    Preparation of melamine thiosulphate and said phosphorus compounds;
    The preparation of some of the phosphorus compounds mentioned initially results, for example, from AT 508.507, AT 508.304 or WO 2011/000018 A1. The phenylphosphonate salts are prepared according to WO 2011/003773, the oligo-gophosphorus compounds or oligophosphines according to WO 2011/029901.
    Further phosphorus compounds and melamine thiosulfate are prepared as follows: 1. Preparation of 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthren-10-one or 10-oxide (DQPO-Om a) Preparation of DOPO-OH in aqueous environment:
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 302.6 g of powdery 9,10-dihydro-9-oxa-10-phosphaphenan-10-thene-10-oxide (DOPO) was suspended in 327.6 g of water Heated 90 CC and within 6 h at a temperature of 90-99 aC with 190.5 g of 30% hydrogen peroxide. The suspension was then cooled to room temperature, the precipitate was filtered off and washed with water. The drying of the filter residue took place at 150.degree. The crude yield was 312.2 g [96.1% d. Th.]. After recrystallization from acetic acid, the following data were determined:
    M.p .: 203 ° C (Lit .: 203-204 ° C, J. Cadogan, supra)
    Elemental Analysis C1ZH903P (M: 232.17 g / mol): calc. C: 62.08%; H: 3.91%; P: 13.34% gef. C: 61.5%; H: 4.2%; P: 13.2% b) Preparation of DOPO-OH in alcoholic-aqueous medium:
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 302.6 g of DOPO were pre-dissolved in 200.0 g of methanol at 25 ° C. and heated continuously to 80 ° C. over 6 h with 317.5 g of 30%. added hydrogen peroxide. The resulting suspension was cooled to room temperature, the precipitate was filtered off and washed with methanol. The drying of the filter residue took place at 150X. The crude yield was 277.1 g [85.3% d. Th.]. After recrystallization from acetic acid, the following data were determined:
    Mp: 203 ° C (Lit .: 203- 204 X); Phosphorus content: gef. 13.3%, over 13.34%. c) Preparation of DOPO-OH in an aromatic-aqueous medium:
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 302.6 g of DOPO was dissolved in 150.0 g of toluene at 70 ° C and with the temperature rising continuously to 85 X within 7 h with 204.1 g of 30% hydrogen peroxide added. Subsequently, 183.7 g of toluene-water mixture were distilled off. The residue was cooled to room temperature and filtered. Drying of the filter residue was carried out at 150 X. The crude yield was 314.9 g [96.9% d. Th.]. After recrystallization from acetic acid, the following data were determined:
    M.p .: 202-203 X (Lit .: 203-204 X); Phosphorus content: gef. 13.2%, over 13.34%. 2. Preparation of 9,10-dihydro-1Q-hydroxy-9-oxa-10-phosphaphenanthren-10-one or 10-oxide-ammonium salt (DOPO-ONHa) a) Liquid process:
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 232.1 g of 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO-OH) in 216.0 g of water suspended and mixed at 25 X with 71.5 g of 25% ammonia. The suspension was then heated to 98 ° C. and then cooled to room temperature. The entire contents of the flask were drained on a drying cup and dried at 120X. The yield was 248.4 g [99.7% d. Th.] Of a white, crystalline solid.
    Mp .: 234-240 X (Zers.)
    Elemental analysis C12Hi2NO3P (M: 249.20 g / mol): calc. C: 57.83%; H: 4.85%; N: 5.62%; P: 12.43% gef. C: 57.5%; H: 5.1%; N: 5.5%; P: 12.4% b) Solid method: 232.0 g of dry and ground DOPO-OH having a grain fineness < 45 pm were placed in a closed grinding chamber and while the shearing work slowly with 78.3 g of ammonia, 25% in water. At the end of the ammonia addition, the millbase had heated to 77 ° C. without losing the powdery state of matter. After a 5-minute mixing time, the shearing unit was stopped and allowed to rest for 1 h. Thereafter, the mixture was reground again for 5 min and then emptied onto a drying cup, distributed and dried at 140 ° C. The yield was 242 g [97.2% d. Th.] Of a white, crystalline solid, the data of which substantially corresponded to those of Example 1. 3. Preparation of 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthren-10-one or -1Q-oxide-melaminium salt (DOPQ-OMel)
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 92.8 g of DOPO-OH were suspended in 400 g of water and mixed at 50 ° C. with 50.4 g of melamine. Subsequently, the suspension was heated to 90 ° C and held for 4 h at this temperature. Thereafter, it was cooled to room temperature. The precipitate was filtered off and washed with water. The drying was carried out at 160 ° C, and the yield was 141.4 g [98.7% d. Th.] Of a white, crystalline solid.
    Mp .: 246-250 ° C (decomp.)
    Elemental Analysis 0.25Η15Ν6θ3Ρ (M: 358.29 g / mol): calc. C: 50.28%; H: 4.22%; N; 23.46%; P: 8.64% gef. C: 49.8%; H: 4.5%; N: 23.3%; P: 8.5% 4. Preparation of 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-one or 10-oxide quanidinium salt (DOPO-OGua)
    In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, a mixture of 100.0 g of water, 100 g of ethanol and 36.0 g of guanidinium carbonate was prepared and heated to 75 ° C. Subsequently, 92.8 g of DOPO-OH were added in portions over a period of 5.5 h. After C02 evolution was no longer detectable, the reaction mass was concentrated by distillation. The remaining crude crystal pulp (135.6 g) was applied to a drying cup and dried at 110 ° C. The yield was 100.5 g [86.0% d, Th.] Of a white, crystalline solid.
    Mp .: 278-280 ° C (Zers.)
    Elemental Analysis C13H14N303P (M: 291.24 g / mol): calc. C: 53.61%; H: 4.84%; N: 14.42%; P: 10.63% gef. C: 53.3%; H: 5.1%; N: 14.3%; P: 10.5% 5. Preparation of Melaminium Thiosulfate (MelTS) a) In a multi-necked flask equipped with stirrer, reflux condenser and thermometer, 1218.7 g of distilled water containing 147.8 g of conc. Hydrochloric acid (37%) and 189.1 g melamine mixed. The suspension was heated to reflux temperature. After a clear solution, the flask contents were cooled to 96 ° C and 348.6 g of a 34% sodium thiosulfate solution. A precipitation reaction occurred. The precipitate was cooled with stirring to room temperature, filtered off and washed thoroughly with distilled water. The drying of the filter residue took place at 110.degree. The yield was 265.1 g [96.5% d. Th.] Of a white, crystalline solid.
    Mp .: 178-180 ° C (Zers.)
    Elemental Analysis C6H14N1203S2 (M: 366.38 g / mol): calc. C: 19.67%; H: 3.85%; N: 45.88%; O: 13.10%; S: 17.50% gef. C: 19.8%; H: 4.0%; N: 45.6%; O: 13.5%; S: 17.2% b) In a multi-necked flask equipped with a stirrer, reflux condenser and thermometer, 1200.0 g of distilled water were added to 252.2 g of melamine and 158.1 g of sodium thiosulfate. The suspension was heated to 95 ° C. Subsequently, at a metering rate of 0.9 g / min, 197.1 g of conc. Hydrochloric acid (37%) was added dropwise. Thereafter, the reaction mass was cooled to room temperature with stirring, the precipitate was filtered off and washed with distilled water. The filter cake was again taken up in 1100 g of distilled water, stirred vigorously and filtered off. The drying of the filter residue took place at 110.degree. The yield was 356.8 g [97.4% d. Th,] of a white, crystalline solid whose data were substantially identical to those of Example 1. c) In a multi-necked flask equipped with stirrer, reflux condenser and thermometer, 1130 g of distilled water, 252.2 g of melamine and 158.1 g of sodium thiosulfate were mixed and heated to 90 ° C. Within 1.5 hours, 174.2 g of 37.5% strength phosphoric acid were added dropwise to the initially charged suspension at 90-93 ° C. Thereafter, the precipitate was cooled while the agitator was running to room temperature and filtered through a Blauband filter. The filter cake was washed with water and then dried at 110.degree. The yield was 328.5 g [89% d. Th.] Of a white, crystalline solid, the data of which substantially corresponded to those of Example 1. • * · · ......... * * * * · »·» # ··· «·· * ·· ·« · I · · * 4 t I * * * «* ♦ ·
    As synergists in the comparative examples were elemental sulfur, Vultac TB7®, a pt-butylphenol disulfide polymer (Arkema), melaminium thiosulfate (bis [(2,4,6-tri-amino-1,3,5-triazinium) thiosulfate, MelTS). (manufactured by Krems Chemie Chemical Services AG) and ammonium thiosulfate ((NH4) 2S203; ATS, Sigma Aldrich).
    These examples enable the person skilled in the art to prepare or obtain the desired flame retardants as such, any required starting materials and also melamine thiosulphate and further synergists.
    Preparation of Expandable Polymers or Poivmerschaumstoffe:
    The preparation of flame-retardant expandable polymers, e.g. of EPS, in the form of granules or beads is known per se to those skilled in the art. The preparation of the polymers according to the invention with the above flame retardants and optionally sulfur compounds works essentially analogously. For example, the embodiments of WO 2006/027241, AT 508.304 or AT 508.507 can be used. The same applies to the polymer foams or XPS,
    EXAMPLES
    The present invention will now be described in detail, by way of example, with reference to some concrete, but non-limiting, embodiments 1, 2, 6, 8, 9, 13, 17 and 18. Examples 3, 4, 5, 7, 10, 11, 12, 14, 15, 16 and 19 are comparative examples:
    Example 1 (Example - MelTS 10.0% + DOPO-ONH4 5.0%):
    A styrene polymer (SUNPOR EPS-STD: 6% by weight of pentane, MW = 200,000 g / mol, nonuniformity MW / Mn = 2.5) in the draw-in area of a twin-screw extruder contained 10% by weight of melamine thiosulfate and 5% by weight of 10-hydroxy-9,10 Dihydro-9-oxa-10-phosphaphenanthren-10-oxide Ammoniurnsalz (DOPO-O-NH4), based on the resulting EPS granules, mixed and melted in the extruder at 190 ° C. The polymer melt thus contained was conveyed through a nozzle plate at a rate of 20 kg / h and granulated with a pressurized underwater granulator to form compact EPS granules.
    Example 2 embodiment - MelTS 6.5% + DOPO-ONHj 3.0%);
    Example 1 was repeated with the difference that 6.5% by weight of melamine thiosulfate and 3.0% by weight of 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide ammonium salt (DOPO-O-NH4) , based on the resulting EPS granules, were added.
    Example 3 (Comparative Example - DQPO-ONKi 15.0%):
    Example 1 was repeated with the difference that only 15.0% by weight of 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthren-10-oxide ammonium salt (DOPO-O-NH4), based on the resulting EPS Granules, were added.
    Example 4 (Comparative Example - DOPO-ONHa 9.5%):
    Example 1 was repeated with the difference that only 9.5% by weight of 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide ammonium salt (DOPO-O-NH4), based on the resulting EPS Granules, were added.
    Example 5 (Comparative Example - MelTS 15.0%):
    Example 1 was repeated with the difference that only 15.0% by weight of melamine thiosulfate (MelTS), based on the resulting EPS granules, were added.
    Example 6 (Embodiment - MelTS 10.0% POPO 5.0%):
    Example 1 was repeated with the difference that 10.0% by weight of melamine thiosulfate and 5.0% by weight of 9,10-dihydro-9-oxa-1Q-phospha-phenanthrene-10-oxide (DOPO), based on the resulting EPS Granules, were added.
    Example 7 (Comparative Example - DOPO 15.0%):
    Example 1 was repeated with the difference that only 15.0% by weight of 9,10-dihydro-9-oxa-10-phospha-phenanthrene-10-oxide (DOPO), based on the resulting EPS granules, were added.
    Example 8 (Exemplary Example - MelTS 10.0% + DOPQ-ONH4 5.0% + graphite 4.0%): Example 1 was repeated with the difference that in addition 4% by weight of microcrystalline natural graphite (UF2 - from Grafit Kropfmühl) in Feeding area of the extruder were added.
    Example 9 (Exemplary Example - MelTS 6.5% + DOPQ-ONHj 3.0% + Graphite 4.0%): Example 2 was repeated with the difference that in addition 4% by weight of microcrystalline natural graphite (UF2 - Grafit Kropfmühl ) were added in the intake area of the extruder.
    Example 1Q (Comparative Example - DOPO-Q-NHa 15.0% + graphite 4.0%):
    Example 3 was repeated with the difference that an additional 4% by weight of microcrystalline natural graphite (UF 2 - from Grafit Kropfmühl) was added in the intake area of the extruder,
    Example 11 (Comparative Example - DOPO-O-NHa 9.5% + graphite 4.0%):
    Example 4 was repeated with the difference that an additional 4% by weight of microcrystalline natural graphite (UF 2 - from Grafit Kropfmühl) was added in the feed zone of the extruder.
    Example 12 (Comparative Example - MelTS 15.0% + graphite 4.0%):
    Example 5 was repeated with the difference that in addition 4% by weight of microcrystalline natural graphite (UF 2 - from Grafit Kropfmühl) were added in the feed zone of the extruder.
    Example 13 (Embodiment - MelTS 10.0% POPO 5.0% + graphite 4.0%):
    Example 6 was repeated with the difference that an additional 4% by weight of microcrystalline natural graphite (UF 2 - from Grafit Kropfmühl) was added in the feed zone of the extruder.
    Example 14 (Comparative Example -POPO 15.0% + graphite 4.0%):
    Example 7 was repeated with the difference that in addition 4% by weight of microcrystalline natural graphite (UF 2 - from Grafit Kropfmühl) were added in the feed zone of the extruder.
    Example 15 (Comparative Example - HBCD 2.5%):
    Example 1 was repeated with the difference that 2.5% by weight Hexabromcyclodode-can (HBCD - FR 1207 Fa. ICL-IP), based on the resulting EPS granules, were added.
    Example 16 (Comparative Example - HBCD 2.5% + graphite 4.0%):
    Example 14 was repeated with the difference that in addition 4% by weight of macrocrystalline natural graphite (UF 2 - from Grafit Kropfmühl), based on the resulting EPS granules, were added.
    Example 17 (Exemplary Example PS / CAB-MelTS 10.0% + DOPO-O-NH4 5.0% + graphite 4.0%):
    A 50:50 mixture of styrene polymer (SUNPOR EPS-STD: 6 wt% pentane, chain length MW = 200,000 g / mol, nonuniformity MW / Mn = 2.5) and cellulose acetate butyrate (CAB 500-5 Fa, Eastman) were used in Feeding range of a twin-screw extruder 10% by weight of melamine thiosulfate (MelTS) and 5.0% by weight of 10-hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide ammonium salt (DOPO-O-NH4), based on the obtained polymer mixture, mixed and melted in the extruder at 190 ° C. The polymer melt thus contained was gassed with 3% pentane isomer mixture (80% n-pentane, 20% iso-pentane) and conveyed through a nozzle plate at a rate of 20 kg / h and granulated with a pressurized underwater granulator to compact foamable granules,
    Example 18 (Exemplary Example PS / CAB Melts 10.0% + DOPQ-O-NHj 5.0% + Graphite 4.0%):
    Example 17 was repeated with the difference that in addition 4% by weight of macrocrystalline natural graphite (UF 2 - from Grafit Kropfmühl), based on the resulting EPS granules, were added,
    Example 19 (Comparative Example PS / CAB - HBCD 2.5% + graphite 4.0%):
    A 50:50 mixture of styrene polymer (SUNPOR EPS-STD: 6 wt% pentane, chain length MW = 200,000 g / mol, nonuniformity MW / Mn = 2.5) and cellulose acetate butyrate (CAB 500-5 Fa. Eastman) were in the catchment area of a Twin screw extruder 2.5% by weight hexabromocyclododecane (HBCD - FR 1207 Fa. ICL-IP) and 4% by weight macrocrystalline natural graphite (UF2 -. Grafit Kropfmühl), based on the polymer mixture obtained, mixed and melted in the extruder at 190 ° C. The polymer melt thus contained was conveyed through a die plate with 3% pentane isomer mixture (80% n-pentane, 20% iso-pentane) at a throughput of 20 kg / h and granulated with a pressurized underwater granulator to form compact foamable granules.
    The following Table 1 shows the results clearly arranged side by side, whereby the fire behavior of defined test specimens, the stability or the time until collapse of the foamed foam beads and the odor were checked.
    Table 1: Testing of the polymers or the polymer foams according to the invention
    Fire test Stability Odor Example 1 Example 1 1 Example 2 Example 2 1 1 Example 3 Comparative Example 3 1 1 Example 5 Comparative Example 5 1 1 Example 6 Example 2 3 1 Example 7 Comparative Example 4 4 1 Example 8 Example 1 1 Example 9 Example 2 1 1 Example 10 Comparative Example 3 1 1 Example 11 Comparative Example 4 1 1 Example 12 Comparative Example 5 1 1 Example 13 Example 2 3 1 Example 14 Comparative Example 4 4 1 Example 15 Comparative Example 1 1 1 Example 16 Comparative Example 1 1 1 Example 17 Example 3 1 2 Example 18 Example 3 1 2 Example 19 Comparative Example 3 1 2
    The results of the experiments in the three right columns were obtained by tests with products of Examples 1 to 19 described above. in detail:
    Fire test (column 3 in Table 1):
    The EPS granules or EPS / CAB granules obtained from the examples were prefoamed with saturated steam to form foam beads having a density of 15 to 25 kg / m 3, stored for 24 hours and shaped into foam sheets in a molded part.
    Test specimens with a thickness of 2 cm were cut from the foam boards, which after 72 hours were subjected to conditioning at 70 ° C. in a fire test in accordance with DIN 4102-2 (B2 small burner test).
    The results rated 1-5 were evaluated relative to He-xabromocyclododecane (HBCD) flame-retarded EPS (Examples 15 and 16). Values of 1 in the column "Fire test" mean that the test substance behaves as well as HBCD-protected EPS with regard to its fire behavior. Values of 5 mean that the reaction to fire is very poor and corresponds to that of non-flame retarded EPS.
    Stability of the foam structures (column 4 in Table 1):
    The EPS granules or EPS / CAB granules obtained from the examples were exposed to saturated water vapor and the time until collapse of the beads occurred determined. This time was evaluated in the summary of results relative to EPS particles without flame retardants. Due to the softening effect of the phosphorus-based flame retardants, the EPS particles showed different stability during prefoaming.
    Where in column " Stability " Values of 1 indicate that the beads have normal stability. Values of 5 mean that the beads immediately collapse without creating a foam structure that would be suitable for molding.
    Odor (column 5 in Table 1):
    The EPS granules or CAB / EPS granules obtained from the examples were prefoamed with saturated water vapor to form foam beads having a density of 15 to 25 kg / m 3, stored for 24 hours and shaped into foam plates in a molding machine.
    Test specimens with a thickness of 2 cm were cut from the foam boards and subjected to a sensory odor test by several laboratory employees. The rating was subjectively according to the criteria "imperceptible" according to the rating 1 to "unpleasant disturbing" with the rating 5.
    Evaluation and discussion of the results fTable 1):
    Examples 1, 2, 6, 8, 9 and 13 show the efficacy of the synergist melamine-thiosulfate in polystyrene foaming in conjunction with phosphorus-based flame retardants based on Comparative Examples 3, 4, 7, 10, 11 and 14, in which the same or higher Concentrations showed worse results in flame retardant properties.
    Examples 5 and 12 show that melamine thiosulfate alone does not have a sufficient flame retardancy and acts as a synergist only in combination with flame retardants, in particular with phosphorus-based flame retardants.
    Examples 15 and 16 are mixed with the flame retardant hexabromocyclododecane (HBCD), which represents the state of the art in polystyrene rigid foams. The results of the two examples were taken as a reference for the evaluation of the fire protection equipment (rating 1 according to the school grading system from 1 to 5).
    Examples 8 to 14 are repetitions of Examples 1 to 7 with the additional equipment with the usual for gray EPS infrared opacifier graphite.
    Examples 17 to 19 are based on a polymer consisting of 50% cellulosic acetate butyrate and 50% polystyrene. Examples 17 and 18 demonstrate the effectiveness of the synergy of melamine thiosulphate and phosphorus based flame retardants in foams based on this polymer matrix.
    Example 19 serves as a comparative example to 17 and 18 in the system Celluloseace-tat / polystyrene.
    In none of the examples was the mechanical stability of the prefoamed granules or of the foam bodies produced therefrom considerably influenced.
    The moldings from Examples 17 to 19 had the typical odor of Cel-luloseacetatbutyrat, which is also detectable on the raw material.
    权利要求:
    Claims (23)
    [1]
    1. Flame-retardant, at least one blowing agent-containing, expandable polymers, characterized in that melaminium thiosulfate (Bis {2,4,6-triamine-1,3,5-triazinium) thiosulfate) NH, S i // -N \ NH- ( NH ΦΘΟ-S-O-θNH / N-λ 0 N -NH, NH, NH, melamine thiosulfate (MelTS) is contained as a flame retardant synergist as part of a flame retardant composition or in combination with at least one flame retardant.
    [2]
    2. Expandable polymers according to claim 1, characterized in that melaminium thiosulfate in an amount of 1 to 25 wt%, in particular in an amount of 2 to 15 wt%, based on the total weight of the polymer is included.
    [3]
    3. Expandable polymers according to claim 1 or 2, characterized in that only halogen-free flame retardants are included.
    [4]
    4. Expandable polymers according to one of the preceding claims, characterized in that at least one phosphorus compound is contained as a flame retardant, wherein the phosphorus compound is selected from elemental phosphorus, in particular red phosphorus, and / or at least one inorganic phosphorus compound or hydrolyzates or salts thereof and / or - At least one organic phosphorus compound of the following general formula (I) or (II) or hydrolyzates or salts thereof: rp: t R, (i) RP = 0 * i R, (II) wherein the radicals R1t R2 and R3 are each independently mean organic or inorganic radicals.
    [5]
    5. Expandable polymers according to one of the preceding claims, characterized in that the flame retardant is a 9,10-dihydro-9-oxa-10-phosphaphenanthren derivative of the general formula (III) or (IIIa) or a salt or ring-opened hydrolyzate thereof

    in which: X is in particular: substituted or unsubstituted C 1 -C 4 -alkyl, C 1 -C 15 -alkenyl, C 3 -C 8 -cycloalkyl, C 6 -C 18 -aryl, C 7 -C 30 -alkylaryl, C 1 -C -alkoxy or C 1 -C 8 -alkylthio, and alkali metal, alkaline earth metal, ammonium or phosphonium salts thereof, and X is in particular selected from -H, -OH, -SH, -ONH, -SNH (Et) 3, -ONH (Et) 3, -Omelamine, guanidine; Y 1t Y 2 and Z each independently represent an oxygen atom or a sulfur atom; n is an integer of at least 1, wherein when Z is an oxygen atom, n = 1, and when Z is a sulfur atom, n = 1 to 8; each of the optional R m groups independently represents an alkyl, alkoxy or alkylthio group having 1 to 8 carbon atoms or an aryl group, and each m is independently an integer of 0 to 4.
    [6]
    6. Expandable polymers according to one of the preceding claims, characterized in that at least one of the following phosphorus compounds is contained as a flame retardant: - Phosphorus compound according to formula (IVa): (IVa)
    10-Hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO-OH) - or salts thereof according to formula (IVb):

    (IVb) (DOPO-OR) - or their ring-opened hydrolysates according to formula (IVc):

    (IVc).
    [7]
    7. Expandable polymers according to claim 6, characterized in that the radical Re is an organic or inorganic cation, in particular a salt of a quaternary ammonium compound NR / or a quaternary phosphonium PR /, is.
    [8]
    8. Expandable polymers according to claim 6 or 7, characterized in that the radical R® in the general formula (IVb) or (IVc) NH4® and the phosphorus compound is 10-hydroxy-9,10-dihydro-9-oxa-10 phosphaphenanthrene 10-oxide ammonium salt: dopo-onh4
    [9]
    9. Expandable polymers according to claim 6 or 7, characterized in that the radical R® in the general formula (IVb) or (IVc) is guanidinium and the phosphorus compound is 10-hydroxy-9,10-dihydro-9-oxa-10 phosphaphenanthrene 10-oxide guanidinium salt:

    , 0 'P * NH. .0 υΘ nr, £. DOPO OGua
    10. Expandable polymers according to claim 6 or 7, characterized in that the radical R®in the general formula (IVb) or (Vlc) is melamine and the phosphorus compound is 10-hydroxy-9,10-dihydro-9-oxa-10 phosphaphenanthrene-1O-oxide melamine salt:







    DOPO OMEL
    11. Expandable polymers according to one of the preceding claims, characterized in that at least one flame retardant is selected from: 9,10-dihydro-9-oxa-10-phosphaphenantrene-10-oxide (DOPO), 9.10-dihydro-9-oxa-10 phosphaphenanthrene-10-thione or 10-sulfide (DOPS), 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione and -10-sulfide (DOPS-OH), 9,10- Dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thion-ammonium salt (D0PS-0NH4) or -10-sulfide-9,10-dihydro-10-mercapto-9-oxa-10-phosphaphenanthrene- 10-thione (DOPS-SH), or -10-sulfide 9,10-dihydro-10-mercapto-9-oxa-10-phosphaphenanthren-10-thione triethylammonium salt (DOPS-SNH (Et) 3), or 10-sulfide-9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione-triethylammonium salt (DOPS-ONH (Et) 3), or -10-sulfide-9,10-dihydro 10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione melaminium salt (DOPS-OMel), or -10-sulfide-9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10 -thione or -10-sulfide guanine dinium salt (DOPS-OGua), 9.10-dihydro-10- (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-ylthio) -9-oxa-10-phosphaphenanthren-10-one or -10-oxide (DOPS-S-DOPO), bis (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) sulfide (DOPS-S-DOPS), bis (9, 10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) disulfide (DOPS-S2-DOPS), bis (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthrene-10 -yl) tetrasulfide (DOPS-S4-DOPS), di (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) ether (DOPS-O-DOPS), 9.10-Dihydro-10 - (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yloxy) -9-oxa-10-phosphaphenanthren-10-one or 10-oxide (DOPS-O-DOPO), Tetraphenyldiphosphine monoxide, tetraphenyldiphosphine monosulfide, tetraphenyl-diphosphine dioxide, tetraphenyldiphosphine disulfide, tetraphenyldiphosphine oxide sulfide, pen-taphenylpentaphospholane, 1,1,3,3-tetramethoxy-2-phenyltriphosphine-1,3-dioxide, 1,1,3,3-tetraethoxy-2-phenyltriphosphine 1,3-dioxide, 1,1,3,3-tetraallyloxy-2-phenyltriphosphine-1,3-dioxide, Melamine Phenylphosphonate salts of formula k

    Where x is a number between or from 1 and 2, guanidine phenylphosphonate salts of the formula NH x h2n nh2

    where x is a number between or of 1 and 2, tetraphenyl resorcinol diphosphate (Fyrolflex® RDP, Akzo Nobel), resorcinol diphosphate oligomer (RDP), triphenyl phosphate, tris (2,4-di-tert-butylphenyl) phosphate, ethylenediamine diphosphates ( EDAP), ammonium polyphosphate, diethyl N, N-bis (2-hydroxyethyl) -amino-methylphosphonate, hydroxyalkyl esters of phosphoric acid, salts of di-C 1-4 alkyl phosphine acids and hypophosphorous acid (H 3 PO 2), in particular the Ca 2+, Zn 2+, o- the AI3 " Salts, tetrakis (hydroxymethyl) phosphonium sulfide, triphenylphosphine and / or phosphazene derivatives.
    12. Expandable polymers according to one of the preceding claims, characterized in that the / the phosphorus compound (s) in an amount of 0.5 to 25 wt .-%, in particular 1 to 15 wt .-%, based on the total weight of the polymer , is / are included.
    13. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers are expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS), which in particular of homo- and copolymers of styrene, preferably glass clear polystyrene (GPPS), impact polystyrene (HIPS), anionically polymerized polystyrene or toughened polystyrene (A-IPS), styrene-alpha-methylstyrene copolymers, acrylonitrile-butadiene-styrene polymers (ABS), styrene-acrylonitrile (SAN) acrylonitrile-styrene-acrylic ester (ASA), methyacrylate-butadiene Styrene (MBS), methyl methacrylate-acrylonitrile-butadiene-styrene (MABS) polymers or mixtures thereof or with polyphenylene ether (PPE).
    14. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers consist of cellulose acetate burtyrate (CAB) or cellulose acetate burtyrate (CAB) and / or that the expandable polymers of polylactic acid (PLA) or contain polylactic acid (PLA).
    15. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers are mixtures of styrene polymers according to claim 13 with expandable thermoplastic polymers such as cellulose acetate burtyrate (CAB), thermoplastic polyurethane (TPU), polylactic acid, etc., wherein the thermoplastic polymers to 1 to 99 wt .-%, based on the total polymer composition, are included,
    16. A process for the preparation of flame-retardant, expandable polymers according to one of the preceding claims, characterized in that melamini-umthiosulfat (Bis ^ Aö-triamine IAS TriaziniurrOthiosulfat) as Flammschutzsynergist as a component of a flame retardant composition or in combination with at least one flame retardant, in particular is used with at least one of the listed in claims 1 to 12 phosphorus compound.
    17. A process for the preparation of flame-retardant expandable polymers, in particular styrene polymers (EPS), according to claim 16, wherein the flame retardant, melaminium thiosulfate and a blowing agent with a polymer melt, in particular a Styrolpolymerschmelze, mixed by means of a dynamic or static mixer and then granulated or wherein the flame retardant and melaminium thiosulfate, by means of a dynamic or static mixer to still granular polymer, in particular polystyrene polymer, are mixed and then the melt is mixed with propellant and granulated or - the flame retardant and melaminium thiosulfate by means of a mixer to granular polymer , in particular polystyrene polymer, are admixed, and the mixture is subsequently melted and granulated, wherein the granule preparation by suspension polymerization, in particular v on styrene, in aqueous suspension in the presence of the flame retardant, of melamine thiosulfate and a propellant.
    18, A process for the preparation of flame-retardant expandable styrene polymers (EPS) according to claim 16 or 17 comprising the steps of: dosing together in an extruder of PS or EPS granules having a molecular weight of Mw > 120 000 g / mol, preferably from 150 000 to 250 000 g / mol, particularly preferably from 180 000 to 220 000 g / mol, and of the flame retardant, melaminium thiosulfate and optionally one or more further additives, in particular a) other flame retardant synergists, eg thermal radical generators, such as dicomyl peroxide, in a concentration of 0.1 to 20% by weight, b) infrared opacifiers, e.g. Graphite, carbon black, petroleum coke, anthracite, aluminum, titanium dioxide, in a concentration of 0.1 to 10% by weight, c) stabilizers, e.g. Nitroxyl radical-forming substances such as HTEMPO (4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl) in a concentration of 0.1 to 1% by weight, d) further halogenated or halogen-free flame retardants, e.g. HBCD, DOP-O, magnesium hydroxide, in a concentration of 0.1 to 20% by weight and / or e) fillers, e.g. Chalk, talc, silicates, in a concentration of 1 to 20 wt% common melting of all components in the extruder, optional metered addition of at least one blowing agent, mixing of all components at a temperature > 120 ° C, granulation by means of pressurized underwater granulation, at e.g. 1-20 bar, to a granule size < 5 mm, preferably 0.2 to 2.5 mm, at a water temperature of 30 to 100 ° C, in particular 50 to 80 ° C, - optionally superficial coating with coating agents, e.g. Silicates, metal salts of fatty acids, fatty acid esters, fatty acid amides.
    19, Flame-retardant, expandable polymers, in particular styrene polymers (EPS), obtainable by a process according to one of Claims 16 to 18.
    20, polymer foam, in particular styrene polymer particle foam or extruded polystyrene foam (XPS) containing melaminium thiosulfate (bis (2,4,6-triamine-1,3,5-triazinium) thiosulfate) as Flammschutzsynergisten as part of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the phosphorus compounds recited in claims 1 to 12.
    21. Polymer foam according to claim 20 obtainable from flame-retardant expandable polymers according to one of claims 1 to 15, in particular from expandable styrene polymers (EPS), in particular by foaming and mixing of the polymers or by extrusion.
    22. A polymer foam according to claim 20 or 21 having a density between 7 and 200 kg / m3 and / or a predominantly closed-cell structure with more than 0.5 cells per mm3, in particular having a structure in which more than 80% of the cells are closed-cell ,
    23. Use of melamine thiosulphate (bis (2,4,6-triamine-1,3,5-triazinium) thiosulphate) as flame retardant synergist as a constituent of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the claims 1 to 12 mentioned phosphorus compounds in expandable polymers, in particular in expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS) or in polymer foams, in particular in styrene polymer particle foams obtainable by foaming from expandable polymers, or in extruded polystyrene rigid foams (XPS). 1. Flame-retardant, at least one blowing agent-containing, expandable polymers, characterized in that melaminium thiosulfate {bis (2,4,6-triamine-1,3,5-triazinium) thiosulfate)

    Melaminium thiosulfate (MelTS) is contained as Flammschutzsynergist as part of a flame retardant composition or in combination with at least one flame retardant. 2. Expandable polymers according to claim 1, characterized in that melaminium thiosulfate in an amount of 1 to 25 wt.%, In particular in an amount of 2 to 15% by weight, based on the total weight of the polymer is included. 3. Expandable polymers according to claim 1 or 2, characterized in that only halogen-free flame retardants are included. 4. Expandable polymers according to one of the preceding claims, characterized in that the flame retardant is at least one phosphorus compound is contained, wherein the phosphorus compound is selected from - elemental phosphorus, in particular red phosphorus, and / or - at least one inorganic phosphorus compound or hydrolyzates or salts thereof and / or - at least one organic phosphorus compound of the following general formula (I) or (II) or hydrolyzates or salts thereof: fl r2-p = o Rz-Pi £ - 1 R, r3 (I) (II) REPLACED 1 t Where R 2 and R 3 are each independently of one another organic or inorganic radicals. 5. Expandable polymers according to one of the preceding claims, characterized in that the flame retardant is a 9,10-dihydro-9-oxa-10-phosphaphenanthren derivative of the general formula (III) or (IIIa) or a salt or ring-opened hydrolyzate thereof

    wherein: X is in particular; substituted or unsubstituted (VCis-alkyl, C 1 -C 5 -alkenyl, C 3 -C 8 -cycloalkyl, C 6 -C 18 -aryl, C 7 -C 30 -alkylaryl, C 1 -C 8 -alkoxy or C 1 -C 6 -alkylthio, and also alkali metal, alkaline earth metal , Ammonium or phosphonium salts thereof, and X is especially selected from -H, -OH, -SH, -ONH4, -SNH (Et) 3, -ONH (Et) 3, -OMelamine, -oguanidine; Yi , Y 2 and Z are each independently an oxygen atom or a sulfur atom; n is an integer of at least 1, wherein when Z is an oxygen atom, n = 1, and when Z is a sulfur atom, n = 1 to 8; the optional radicals R m each independently represent an alkyl, alkoxy or alkylthio group having 1 to 8 carbon atoms or an aryl group and m each independently represents an integer from 0 to 4. Expandable polymers according to one of the preceding claims, characterized in that at least one of the following phosphorus compounds is contained as flame retardant t: - phosphorus compound according to formula (IVa):

    [10]
    10-Hydroxy-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOPO-OH) - or salts thereof according to formula (IVb):

    (IVb) (DOPOOR) - or their ring-opened hydrolysates according to formula (IVc): r S / 0 OH OH (IVc). 7. Expandable polymers according to claim 6, characterized in that the radical R® is an organic or inorganic cation, in particular a salt of a quaternary ammonium compound NR / or a quaternary phosphonium PR4 +, is. 8. Expandable polymers according to claim 6 or 7, characterized in that the radical R® in the general formula (IVb) or (IVc) NH4® and the phosphorus compound is lO-Hvdroxy-g.lO-dihydro-g-oxa-IO -phosphaphenanthren-IO-oxide-AmiTinP8 "™ 1 ^ 1- ^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^ 4 • · • · ······ «4 # · ·· ♦ · * ·« «··« · «

    9.nh4 DOPO-ONH4 9. Expandable polymers according to claim 6 or 7, characterized in that the radical R® in the general formula (IVb) or (IVc) guanidinium and the phosphorus compound is 10-hydroxy-9,10-dihydro-9 -oxa-10-phosphaphenanthrene-10-oxide-guanidinium salt: p ^ 0 NHL I " Ολ 'X

    10. Expandable polymers according to claim 6 or 7, characterized in that the radical R® in the general formula (IVb) or (Vlc) is melamine and the phosphorus compound is 10-hydroxy-9,10 dihydro-9-oxa-10-phosphaphenanthrene 10-oxide melamine salt:

    e NH "NH. DOPO-OMel FOLLOWED
    [11]
    | 11. Expandable polymers according to one of the preceding claims, characterized in that at least one flame retardant is selected from: 9,10-dihydro-9-oxa-10-phosphaphenantrene-10-oxide (DOPO), 9.10-dihydro-9-oxa-10 phosphaphenanthrene-10-thione or 10-sulfide (DOPS), 9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione and -10-sulfide (DOPS-OH), 9,10- Dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thion-ammonium salt (DOPS-ONH4), or -10-sulfide-9,10-dihydro-10-mercapto-9-oxa-10-phosphaphenanthrene- 10-thione (DOPS-SH), or -10-sulfide 9,10-dihydro-10-mercapto-9-oxa-10-phosphaphenanthren-10-thione triethylammonium salt (DOPS-SNH (Et) 3), or 10-sulfide-9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione-triethylammonium salt (DOPS-ONH (Et) 3), or -10-sulfide-9,10-dihydro 10-hydroxy-9-oxa-10-phosphaphenanthrene-10-thione melaminium salt (DOPS-OMel), or -10-sulfide-9,10-dihydro-10-hydroxy-9-oxa-10-phosphaphenanthrene-10 -thione or -10-sulfide-guan idinium salt (DOPS-OGua), 9,10-dihydro-10- (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-ylthio) -9-oxa-10-phosphaphenanthren-10-one or 10-oxide (DOPS-S-DOPO), bis (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) sulfide (DOPS-S-DOPS), bis (9,10 -dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) disulfide (DOPS-S2-DOPS), bis (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthrene-10 yl) tetrasulfide (DOPS-S4-DOPS), di (9,10-dihydro-9-oxa-10-phospha-10-thioxophenanthren-10-yl) ether (DOPS-O-DOPS), 9.10-Dihydro-10 (9,10-dihydro-9-oxa * 10-phospha-10-thioxophenanthren-10-yloxy) -9-oxa-10-phosphaphenanthrene-10-one or 10-oxide (DOPS-O-DOPO), tetraphenyldiphosphine monoxide , Tetraphenyldiphosphine monosulfide, tetraphenyl-diphosphine dioxide, tetraphenyidiphosphine disulfide, tetraphenyldiphosphine oxide sulfide, penaphenylpentaphospholane, 1,1,3,3-tetramethoxy-2-phenyltriphosphine-1,3-dioxide, 1,1,3,3-tetraethoxy-2-phenyltriphosphine 1,3-dioxide, 1,1,3,3-tetraallyloxy-2-phenyltriphosphine-1,3-dioxide, Melamine Phenylphosphonate Salts of the Formula I Subsequent 6 • ······················································

    Ο

    Where x is a number between or 1 and 2, guanidine phenylphosphonate salts of the formula H2N



    where x is a number between and from 1 and 2, tetraphenyl resorcinol diphosphate {Fyrolflex® RDP, Akzo Nobel), resorcinol diphosphate oligomer (RDP), triphenyl phosphate, tris (2,4-di-tert-butylphenyl) phosphate, ethylenediamine diphosphates (EDAP), ammonium polyphosphate, diethyl N, N-bis (2-hydroxyethyl) amino methyl phosphonate, hydroxyalkyl esters of phosphoric acid, salts of di-C 1 -C 4 alkyl phosphine acids and hypophosphorous acid (H 3 PO 2), especially Ca 2+, Zn 2+, o-the AI3 * salts, tetrakis (hydroxymethyl) phosphonium sulfide, triphenylphosphine and / or phosphazene derivatives.
    [12]
    12. Expandable polymers according to one of the preceding claims, characterized in that the / the phosphorus compound (s) in an amount of 0.5 to 25 wt .-%, in particular 1 to 15 wt .-%, based on the total weight of the polymer , is / are included.
    [13]
    13. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers are expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS), which in particular of homopolymers and copolymers of styrene, preferably glassy polystyrene (GPPS), beat -zähpoiystyrol (HIPS), anionically polymerized polystyrene or impact polystyrene (A-IPS), styrene-alpha-methylstyrene copolymers, acrylonitrile-butadiene-styrene polymers (ABS), styrene-acrylonitrile (SAN) acrylonitrile-styrene-acrylic ester (ASA), methyl acrylate Butadiene-styrene (MBS), methyl methacrylate-acrylonitrile-butadiene-styrene (MABS) polymers or mixtures thereof or with polyphenylene ether (PPE). SUBSEQUENT
    [14]
    14. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers consist of Celiuloseacetatburtyrat (CAB) or Celiuloseacetatburtyrat (CAB) and / or that the expandable polymers of polylactic acid (PLA) exist or polylactic acid (PLA).
    [15]
    15. Expandable polymers according to one of the preceding claims, characterized in that the expandable polymers are mixtures of styrene polymers according to claim 13 with expandable thermoplastic polymers, such as Cellulo-seacetatburtyrat (CAB), thermoplastic polyurethane (TPU), polylactic acid, etc., wherein the thermoplastic Polymers to 1 to 99 wt .-%, based on the total polymer composition, are included.
    [16]
    16. A process for the preparation of flame-retardant, expandable polymers according to any one of the preceding claims, characterized in that melamini-umthiosulfat (bis (2,4,6-triamine-1,3,5-triazinium) thiosulfate) as a flame retardant synergist as part of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the listed in claims 1 to 12 phosphorus compound is used.
    [17]
    17. A process for the preparation of flame-retardant expandable polymers, in particular styrene polymers (EPS), according to claim 16, wherein the flame retardant, melaminium thiosulfate and a blowing agent with a polymer melt, in particular a Styrolpolymerschmelze, mixed by means of a dynamic or static mixer and then granulated or wherein the flame retardant and melaminium thiosulfate, by means of a dynamic or static mixer to granuiatförmigem polymer, in particular polystyrene polymer, are admixed and melted, and the melt is then mixed with propellant and granulated or - wherein the flame retardant and melamine thiosulfate by means of a mixer to granular polymer , in particular polystyrene polymer, are admixed, and the mixture is then melted and granulated

    FOLLOW-ON OR if the preparation of granules is effected by suspension polymerization, in particular of styrene, in aqueous suspension in the presence of the flame retardant, of melamine thiosulphate and a propellant.
    [18]
    18. Process for the preparation of flame-retardant expandable styrene polymers (EPS) according to claim 16 or 17 comprising the steps of: dosing together in an extruder of PS or EPS granules having a molecular weight of Mw > 120 000 g / mol, preferably from 150 000 to 250 000 g / mol, particularly preferably from 180 000 to 220 000 g / mol, and of the flame retardant, melaminium thiosulfate and optionally one or more further additives, in particular a) other flame retardant synergists, eg thermal radical generators, such as dicomyl peroxide, in a concentration of 0.1 to 20% by weight, b) infrared opacifiers, e.g. Graphite, carbon black, petroleum coke, anthracite, aluminum, titanium dioxide, in a concentration of 0.1 to 10% by weight, c) stabilizers, e.g. Nitroxyl radical-forming substances such as HTEMPO (4-hydroxy-2,2,6,6-tetramethylpiperidine-1-oxyl) in a concentration of 0.1 to 1% by weight, d) further halogenated or halogen-free flame retardants, e.g. HBCD, DOP-O, magnesium hydroxide, in a concentration of 0.1 to 20% by weight and / or e) fillers, e.g. Chalk, talc, silicates, in a concentration of 1 to 20% by weight - joint melting of all components in the extruder, optional metering of at least one blowing agent, mixing of all components at a temperature > 120 ° C, granulation by means of pressurized underwater granulation, at e.g. 1-20 bar, to a granule size < 5 mm, preferably 0.2 to 2.5 mm, at a water temperature of 30 to 100 ° C, in particular 50 to 80 ° C, - optionally superficial coating with coating agents, e.g. Silicates, metal salts of fatty acids, fatty acid esters, fatty acid amides.
    [19]
    19. Flame-retardant, expandable polymers, in particular styrene polymers (EPS), obtainable by a process according to one of Claims 16 to 18,
    [20]
    20. Polymer foam, in particular styrene polymer particle foam or extruded polystyrene rigid foam (XPS), containing melaminium thiosulphate (bis (2,4,6-triamine-I NACHGB 1,3,5-triazinium) thiosulphate) as flame retardant synergists as constituent of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the phosphorus compounds recited in claims 4 to 12.
    [21]
    21. Polymer foam according to claim 20 obtainable from flame-retardant expandable polymers according to one of claims 1 to 15, in particular from expandable styrene polymers (EPS), in particular by foaming and mixing of the polymers or by extrusion.
    [22]
    22. Polymer foam according to claim 20 or 21 having a density between 7 and 200 kg / m3 and / or a predominantly closed-cell structure with more than 0.5 cells per mm3, in particular with a structure in which more than 80% of the cells are closed. are cellular.
    [23]
    23. Use of melaminium thiosulfate (bis {2,4) -6-triamine-1,3,5-triazinium) thiosulfate) as a flame retardant synergist as a constituent of a flame retardant composition or in combination with at least one flame retardant, in particular with at least one of the claims 4 to 12 mentioned phosphorus compounds in expandable polymers, in particular in expandable styrene polymers (EPS) or expandable styrene polymer granules (EPS) or - in polymer foams, in particular in styrene polymer particle foams, obtainable by foaming from expandable polymers, or in extruded polystyrene rigid foams (XPS) , Vienna, March 27, 2012 SUBSCRIBED j
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    法律状态:
    2016-12-15| MM01| Lapse because of not paying annual fees|Effective date: 20160418 |
    优先权:
    申请号 | 申请日 | 专利标题
    AT5452011A|AT511090B1|2011-04-18|2011-04-18|FLAME-PROOF EXPANDABLE POLYMERISATE|AT5452011A| AT511090B1|2011-04-18|2011-04-18|FLAME-PROOF EXPANDABLE POLYMERISATE|
    EP12720389.1A| EP2699634A1|2011-04-18|2012-04-17|Flame-retardant expandable polymers|
    PCT/AT2012/000103| WO2012142634A1|2011-04-18|2012-04-17|Flame-retardant expandable polymers|
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