The present invention relates to flame retarded expandable vinyl aromatic polymers, their production and foams produced therefrom.
Expanded vinyl aromatic foams, in particular polystyrene foams have been known for a long time and have numerous applications in many fields. Such foams are produced by heating polystyrene particles impregnated with blowing agents to achieve an expansion in a mold where the expanded particles are welded together to achieve molded parts. A significant application area of such molded panels is thermal insulation in building and construction.
It is known that the thermal conductivity of foams can be reduced by incorporation of athermanous materials such as carbon black, coke, graphite, metal oxides, metal powder or pigments
The incorporation of thermal insulation increasing material in expandable vinyl aromatic polymers is disclosed for example in EP 1486530, EP 620246, EP 0915127, EP1945700, EP 1877473, EP 2274370, EP 2358798, EP 2454313, EP 372343, EP 674674, EP 902804, EP 863175, EP 1137701, EP 1102807, EP 0981575, EP 2513209, EP0915127, DE 19910257, DE 202010013850, US 2011/213045, WO97/45477, WO9851735, WO 2004/087798, WO 2008/061678, WO 2010/128369, WO 2010/141400, WO 2011/042800 and WO 2011/133035, WO 2011/110333, WO2011/122034, WO 2013/064444, WO 2014/102139, WO 2014/063993, WO 2014/102137, WO 2014/122190 and JP 2005002268.
Styrene-based polymers have the property of burning vigorously with evolution of black smoke once ignited. For this reason, it is imperative to flameproof the polymers by the addition of a flame retardant in order to be endowed with fire resistance properties that enable to have a good rating according to the DIN 4102-1 (B1 or B2), EN ISO 11925-2, EN ISO 13823 and EN ISO 13501-1.
The flame-retardant agents particularly suitable for being used in the expandable vinyl aromatic compositions are chlorinated and/or brominated aliphatic, cyclo-aliphatic and aromatic compounds.
Flame retardants in which all of bromine atoms are bonded to aliphatic carbon, such as hexabromocyclododecane have already clearly demonstrated their efficiency.
Since hexabromocyclododecane has a bioaccumulation property, is toxic for aquatic organisms, and is hardly decomposed, a brominated polymer type flame retardant is considered as a substitute.
Brominated polymers, in particular brominated block copolymers, for use as flame retardant in expandable vinyl aromatic polymers are disclosed in for example WO 2014/027888 and WO 2013/009469.
However, the brominated polymer type flame retardants have insufficient thermal stability, and may be thermally deteriorated, causing black foreign substances or discoloration, when exposed to a high temperature and residence time, such as for example in a process for mixing the brominated polymer type flame retardant with a styrene-based polymer to manufacture a flame-retardant resin composition in an extrusion process.
Thermally stable brominated copolymers are disclosed in EP 1 957 544.
Thermal stability of halogenated flame retardants, in general, has been improved through the introduction of acid scavengers such a metal salts, triazine and epoxy containing organic compounds among others.
EP 2 379 628 discloses aliphatic bromine containing polymers, stabilized using a mixture of an alkylphosphite and an epoxy compound. The stabilizer package is very effective for the polymer subjected to high temperatures as are seen in melt processing operations.
EP 2 998 347 discloses a recyclable flame-retardant expandable styrene resin composition having a high flame retardancy and thermal stability with a small amount of a bromine-containing flame retardant added. The flame-retardant expandable styrene resin composition contains (A) a styrene resin, (B) a bromine-containing organic compound, (C) zinc oxide, and (D) a foaming agent, wherein an amount of (C) is less than 2 parts by weight per 100 parts by weight of (A) the styrene resin. The flame-retardant expandable styrene resin composition can further contain (E) a thermal stabilizer. Examples of the thermal stabilizer include a phosphite compound, a thioether compound, a hindered phenol compound, a hindered amine compound, an organic tin compound, a phosphoric acid ester, and hydrotalcite.
EP 3 301 134 discloses a flame-retardant resin composition, for extrusion molding, containing 0.8 to 15 parts by mass of a halogen capture agent, 0.8 to 7 parts by mass of an antioxidant, and 0.8 to 6 parts by mass of liquid paraffin based on a total of 100 parts by mass of a styrene-based resin and brominated polymer type flame retardant wherein the content of bromine is 18 to 42% by mass. Examples of halogen capture agent include a dolomite-based compound, a hydrotalcite-based compound. The hydrotalcite-based compound is one kind of naturally produced clay minerals represented by Mg6Al2(OH)16CO3.nH2O or the like.
EP 2 921 520 discloses a recyclable flame-retardant foamed styrene resin composition having high flame-retardancy and heat stability by adding little bromine-containing flame retardant. A flame-retardant foamed styrene resin composition containing (A) a styrene resin, (B) a mixture of (B1) tetrabromobisphenol A-bis(2,3-dibromo-2-methylpropyl ether) and (B2) another bromine-containing flame retardant, (C) zinc-modified hydrotalcite, (D) zeolite, and (G) a foaming agent, containing 0.005-0.08 parts by weight of (C) per 100 parts by weight of (A) the styrene resin.
Without being limitative, the interaction of athermanous material with the flame retardant and/or its synergist is a major issue since higher amounts of flame retardant have some times to be introduced in the expandable styrene polymer in order to have a good rating (B1 or B2) according to the DIN 4102-1 test, and the single burning item (SBI) test according EN 13823 and classified according to EN 13501-1. All athermanous additives have a certain influence on the cell formation and thus on expansion capabilities, density and open cell rate which again influences fire resistance and thermal conductivity.
Without contesting the associated advantages of the state of the art systems, it is nevertheless obvious that there is still a need for expandable vinyl aromatic polymers, intended for thermal insulation in building and construction applications wherein outstanding insulation properties are combined with good flame retardancy obtained from the incorporation of the lowest possible amounts of non-toxic, environmental safe flame retardants.
The present invention aims to provide expandable vinyl aromatic polymers enabling the production of expanded beads allowing molded parts such as insulation panels with an improved fire resistance at lower flame retardant concentrations and simultaneously a reduced thermal conductivity obtained in an economically attractive and a safe way.
The present invention discloses an expandable vinyl aromatic polymer composition comprising:
Preferred embodiments of the present invention disclose one or more of the following features:
[MgaZnbAlx(OH)2]x+(An−)x/n.mH2O,
The present invention further discloses a method for the preparation of beads or granules of the expandable vinyl aromatic polymer, comprising the steps of:
Preferred embodiments of the process for the preparation of beads or granules of the expandable vinyl aromatic polymer disclose one or more of the following features:
The present invention additionally discloses polymer foams obtained from the molding of the expanded vinyl aromatic polymers obtained by the expansion of the expandable vinyl aromatic polymer composition said foams being characterized by:
It is an object of the present invention to provide expandable vinyl aromatic polymer compositions, which can be processed to expanded foams which have both a low density and a low thermal conductivity, good processing properties and, in particular, very good flame retardant properties.
The present invention provides a flame-retardant foamable vinyl aromatic polymer composition comprising a vinyl aromatic polymer, athermanous particles, halogenated flame retardant and zinc-modified hydrotalcite.
The vinyl aromatic polymers preferably used in the present invention comprise glass-clear polystyrene (GPPS), impact-resistant polystyrene (HIPS), anionically polymerized polystyrene or impact-resistant polystyrene (AIPS), styrene-alpha-methylstyrene copolymers, acrylonitrile-butadiene-styrene polymers (ABS), styrene-acrylonitrile polymer (SAN), acrylonitrile-styrene-acrylate (ASA), styrene acrylates, such as styrene-methyl acrylate (SMA) and styrene-methyl methacrylate (SMMA), methyl methacrylate-butadiene-styrene (MBS), methyl methacrylate-acrylonitrile-butadiene-styrene (MABS) polymers, styrene-N-phenylmaleimide copolymers (SPMI) or a mixture thereof, or a mixture of the above-mentioned styrene polymers with polyolefins, such as polyethylene or polypropylene, and polyphenylene ether (PPE).
The weight average molecular weight of the expandable vinyl aromatic polymers, in particular styrene polymers, of the present invention is preferably in the range from 120,000 to 400,000 g/mol, particularly preferably in the range from 160,000 to 300,000 g/mol, measured by means of gel permeation chromatography against polystyrene standards. The molar mass of the expandable vinyl aromatic polymers, in particular styrene polymers, in the extrusion processes is generally below the molar mass of the vinyl aromatic polymers, in particular of the polystyrene, used, by 10,000 g/mol, because of the degradation of molar mass caused by shear and/or by heat.
The abovementioned vinyl aromatic polymers, in particular styrene polymers, can be blended with thermoplastic polymers, such as polyamides (PA), polyolefins, e.g. polypropylene (PP) or polyethylene (PE), polyacrylates, e.g. polymethyl methacrylate (PMMA), polycarbonate (PC), polyesters, e.g. polyethylene terephthalate (PET) or polybutylene terephthalate (PBT), polyether sulfones (PES), polyether ketones, or polyether sulfides (PES), or a mixture thereof, generally in total proportions of up to at most 30% by weight, preferably in the range from 1 to 10% by weight, based on the polymer melt, in order to improve mechanical properties or heat resistance, optionally with use of compatibilizers. Mixtures within the abovementioned ranges of amounts are also possible with, for example, hydrophobically modified or functionalized polymers or oligomers, rubbers, e.g. polyacrylates or polydienes, for example styrene-butadiene block copolymers, or biodegradable aliphatic or aliphatic/aromatic copolyesters.
The athermanous particles preferably comprise carbon black, coke, graphite or a combination thereof. The athermanous particles for being used in the expandable vinyl aromatic polymers of the present invention are characterized by a particle size distribution, as determined by laser diffraction according to ISO 13320 using MEK as solvent for vinyl aromatic polymers, with a volume median particle diameter (D50) comprised between 0.5 and 35 μm, preferably between 0.8 and 20 μm, more preferably between 0.8 and 20 μm and more preferably between 1 and 10 μm and are present in an amount comprised between 0.5 and 15 parts by weight, preferably between 1 and 10 parts by weight for 100 parts by weight of vinyl aromatic polymer.
The technique of laser diffraction is based on the principle that particles passing through a laser beam will scatter light at an angle that is directly related to their size: large particles scatter at low angles, whereas small particles scatter at high angles. The laser diffraction is accurately described by the Fraunhofer approximation and the Mie theory, with the assumption of spherical particle morphology.
A sample presentation system ensures that the material under test passes through the laser beam as a homogeneous stream of particles in a known, reproducible state of dispersion, for particle concentrations adjusted to have a suitable transmission percentage.
The particle size distribution has been measured by laser light scattering using the particle size analyzer (HORIBA 920) from (Horiba Scientific) according to ISO 13320. For Horiba 920, the suitable transmission percentage is situated between 70 and 95.
Specific examples of bromine-containing flame retardant include hexabromocyclododecane, tris(2,3-dibromopropyl) isocyanurate, tetrabromobisphenol 5-bis(2,3-dibromopropyl ether), tetrabromobisphenol F-bis(2,3-dibromopropyl ether), tetrabromobisphenol A, hexabromobenzene, pentabromotoluene, polybromodiphenyl ether, polybromodiphenylethane, bispolybromophenoxyethane, tris(tribromophenoxy)triazine, polybromophenylindan, polypentabromobenzyl acrylate, ethylenebistetrabromophthalimide, tris(tribromoneopentyl) phosphate, brominated epoxy resin oligomers and mixtures of two or more bromine-containing flame retardants.
Preferably the flame retardant for being used in the expandable vinyl aromatic compositions of the present invention is chosen from tetrabromobisphenol A-bis(2,3-dibromopropyl ether), tetrabromobisphenol A-bis(2,3-dibromo-2-methylpropyl ether) or brominated polymers, present in an amount of from 0.2 to 5 parts by weight, preferably of from 0.3 to 4 parts by weight, more preferably from 0.4 to 3 parts by weight per 100 parts of vinyl aromatic polymer.
More preferably the flame-retardant agents for being used in the expandable vinyl aromatic compositions of the present invention are brominated block copolymers obtained from the bromination of block copolymers comprising from 20 to 60% by weight, preferably from 30 to 50% by weight of sequences (A) of polymerized monovinyl arenes and from 40 to 80% by weight, preferably from 50 to 70% by weight of sequences (B) of polymerized conjugated alkadienes or copolymerized conjugated alkadienes and monovinyl arenes, said brominated block copolymers comprising from 20 to 80% by weight, preferably from 40 to 70% by weight of bromine.
The mono vinyl arene units preferably are styrene units formed by polymerizing styrene. However, other mono vinyl arene units can be present, such as α-methyl styrene, 2-, 3- or 4-methyl styrene, other alkyl-substituted styrenes such as ethyl styrene. Mixtures of two or more different types of mono vinyl arene units can be present.
The block copolymers are further characterized by a weight average molecular weight comprised between 20,000 and 300,000 g/mol, preferably between 30,000 and 200,000 g/mol as determined by gel permeation chromatography against polystyrene standards.
The halogenated block copolymer may be a diblock copolymer or triblock copolymer. A triblock copolymer preferably includes a central block of sequence (B) with terminal blocks of sequence (A).
Brominated block copolymers containing at least 35% by weight bromine are preferred.
At least 90%, of the bromine is bonded to the monomer units of sequence (B). As much as 100% of the bromine may be bonded the monomer units of sequence (B).
Preferably the halogenated block copolymer is a brominated styrene-butadiene block copolymer.
The brominated vinyl aromatic-butadiene block copolymer preferably is a diblock copolymer, more preferably triblock copolymer including a central polybutadiene block with terminal blocks of the polymerized vinyl aromatic monomer.
Brominated vinyl aromatic-butadiene block copolymers containing at least 45% by weight bromine are preferred.
Bromination produces brominated 1,2-butadiene and 1,4-butadiene units.
The brominated vinyl aromatic-butadiene copolymers may be produced as for example described, in WO 2008/021417, WO 2010/114637, WO 2009/134628, WO 2008/021418 and WO 2008/021418.
The brominated vinyl aromatic-butadiene copolymer should have a 5% weight loss temperature of at least 200° C., preferably at least 220° C., more preferably at least 240° C. and most preferably at least 250° C. The 5% weight loss temperature is preferably no greater than 300° C., more preferably no greater than 280° C. 5% weight loss temperature is measured by thermogravimetric analysis (TGA).
The expandable vinyl aromatic polymer compositions of the present invention comprise between 0.2 and 5 parts by weight, preferably between 0.3 and 4 parts by weight more preferably between 0.4 and 3 parts by weight of the halogenated polymers, preferably brominated block copolymers, per 100 parts by weight of the vinyl aromatic polymer.
The effectiveness of the halogenated fire retardant agent can be still further improved via addition of suitable flame retardant synergists, examples being the thermal free-radical generators of the type comprising a C—C or C—O—O—C or S—S thermo-labile bond
Examples of such a radical generator include cumene peroxide, cumene hydroperoxide, di-tert-butyl peroxide, di-tert-hexylperoxide, 2,5-dimethyl-2,5-di(tert-butylperoxy)hexyne-3, dicumyl peroxide, and 2,3-dimethyl-2,3-diphenylbutane. Dicumyl peroxide and 2,3-dimethyl-2,3-diphenylbutane are preferred. Flame retardant synergists are generally used in amounts of from 0.05 to 5 parts by weight, preferably in amounts of from 0.1 to 3 parts by weight per 100 parts of vinyl aromatic polymer.
The heat stabilizer for being used in the expandable vinyl aromatic compositions of the present invention is zinc-modified hydrotalcite, a layered double hydroxide resulting from replacement of part of Mg of hydrotalcite Mg6Al2(OH)16(CO3).4H2O with Zn and is represented by the formula [MgaZnbAlx(OH)2]x+(An−)x/n.mH2O, wherein 0.5≤a+b<1.0; 0<x≤0.5 and a+b=1−x; and a≤b>0.03 a; preferably a≤b>0.3 a; m is a positive number, and A is an n-valent anion. Preferably, the anion is carbonate ion CO32−.
The zinc-modified hydrotalcite having the formula Mg3ZnAl2(OH)12CO3.mH2O is available from Kisuma Chemical Industry Co., Ltd. under the trade name of ZHT-4V, and the zinc-modified hydrotalcite having the formula Mg35Zno5Al2(OH)12CO3.3H2O is available from Sakai Chemical Industry Co., Ltd. under the trade name of STABIACE HT-7 and from Kisuma Chemical Industry Co., Ltd. Under the trade name ZT-100. Zinc-modified hydrotalcite differing in atomic ratios of Mg and Zn to Al from these commercially available products can be synthesized from a water-soluble salt of Mg, Zn and Al by a known method called a coprecipitation method.
The zinc-modified hydrotalcite further is characterized by a particle size distribution, as determined by the laser light scattering granulometry technique, with a volume median particle diameter (D50) comprised between 0.1 and 15 μm, preferably between 0.1 and 10 μm, more preferably between 0.1 and 8 μm.
Zinc-modified hydrotalcite is added in an amount of 1 to 50 parts by weight, preferably 1 to 40 parts by weight, more preferably 1 to 30 parts by weight, most preferably 1 to 25 parts by weight per 100 parts by weight of halogenated polymer.
The zinc-modified hydrotalcite is preferably treated with a surface treatment agent for enabling its uniform dispersion in a vinyl aromatic polymer composition. Examples of such a surface treatment agent include higher fatty acids such as stearic acid, oleic acid, and lauric acid, higher fatty acid metal salts such as sodium stearate and sodium oleate, anionic surfactants such as sodium laurylbenzenesulfonate, silane coupling agents such as vinyltriethoxysilane and gamma-methacryloylpropyltriethoxysilane, titanate coupling agents such as isopropyltriisostearoyl titanate and isopropyltridecylbenzenesulfonyl titanate, glycerin fatty acid esters such as glycerin monostearate and glycerin monooleate, higher fatty acid amides such as stearic acid amide, and waxes.
To the flame-retardant vinyl aromatic polymer composition of the present invention additional stabilizers may further be blended. Blends of the heat stabilizer can further improve heat stability. Examples of such further stabilizers include phosphite compounds, thioether compounds, hindered phenol compounds, hindered amine compounds, organotin compounds, phosphates, and hydrotalcite.
Hydrotalcite compounds having the formula [Mg1-x Alx (OH)2]X+(CO3)x/2.mH2O wherein 0<x≤0.5, and m is a positive number, can also be added as an additional heat stabilizer. As one example, synthetic hydrotalcite having the formula Mg4.3Al2(OH)12.6CO3.mH2O is available from Kyowa Chemical Industry Co., Ltd. under the trade name of DHT-4A.
When using the additional stabilizers, the addition amount thereof is up to 50 parts by weight, preferably up to 40 parts by weight, more preferably up to 30 parts by weight, most preferably up to 20 parts by weight per 100 parts by weight of the halogenated polymer.
Expandable vinyl aromatic polymers further generally comprise, per 100 parts of vinyl aromatic polymer, 2 to 10 parts by weight, preferably 3 to 7 parts by weight, of one or more blowing agents distributed homogeneously. Suitable blowing agents are the physical blowing agents usually used in expandable styrene polymers e.g. aliphatic hydrocarbons having from 2 to 7 carbon atoms, alcohols, ketones, ethers, or halogenated hydrocarbons. Preferred blowing agents are isobutane, n-butane, isopentane, or n-pentane.
Various kinds of cell regulators working according to various mechanism are known in the field of polymer foams. Inert particles at polymer melt temperatures such as talc; titanium dioxide; clays such as kaolin; silicagel; calcium polysilicate; gypsum; metal particles; calcium carbonate; calcium sulfate; magnesium carbonate; magnesium hydroxide; magnesium sulfate; barium sulfate; diatomaceous earth; nano-particles such as nano-particles of calcium carbonate, nano clay and nano-graphite work by adsorbing microscopic (mainly liquid) blowing agent particles and improving the dispersion of those particles in the polymer matrix.
Various molecules, the so-called nucleating agents, are also known as cell regulators. Typical products are esters of abietic acids, polyoxyethylene sorbitan monolaurate, Montan wax, Candelilla wax, Carnauba wax, Paraffine wax, Ceresine wax, Japan wax, Petrolite wax, Ceramer wax, polyethylene wax, polypropylene wax and mixtures thereof.
A foam cell regulator of particular interest within the scope of the present invention comprises polyethylene wax.
Examples of polyethylene wax, particularly suitable to be used in the expandable vinyl aromatic compositions, are high density polyethylene waxes characterized by a weight average molecular weight in the range of from 1,500 to 5,000 g/mol and a polydispersity (Mw/Mn) of less than 2.0, preferably less than 1.3, more preferably less than 1.2.
The foam cell regulator is added in such a way that the final expandable vinyl aromatic polymer comprises between 0.01 and 2.0 parts by weight, preferably between 0.05 and 1.0 parts by weight of polyethylene wax per 100 parts of vinyl aromatic polymer.
The expandable vinyl aromatic polymers further can comprise the usual and known auxiliaries and additives, examples being, fillers, UV stabilizers, chain-transfer agents, plasticizers, antioxidants, soluble and insoluble inorganic and/or organic dyes and pigments.
Various processes can be used to produce the particularly preferred expandable vinyl aromatic polymers. After the polymerization process, the melt stream is divided into a first polymer melt stream 1 and a second polymer melt stream 2 (
In a preferred embodiment, comminuted athermanous particles are taken as starting point together with foam cell regulator. These components are simultaneously fed into the second polymer melt stream 2 of the vinyl aromatic polymer via a mixing unit C, preferably via an extruder. To the first polymer melt stream 1, blowing agent is added from unit D. After dispersion of the first additive package, said second polymer melt stream 2 joins again the first polymer stream 1, comprising blowing agent, to form the new joint polymer melt stream, preferably through a static mixer E.
The vinyl aromatic polymer melt comprising blowing agent, athermanous particles, foam cell regulator and in a later stage flame retardant agent, synergist and heat stabilizer, after homogenization, is rapidly cooled under pressure, in order to avoid foaming. It is therefore advantageous to carry out underwater pelletizing in a closed system under pressure.
Particular preference is given to a process for producing flame-retarded, expandable vinyl aromatic polymers, comprising the steps of:
The expandable pellets (beads, granules) can then further be coated and processed to give expanded vinyl aromatic polymer foams, in particular polystyrene foams
In a first step, the expandable vinyl aromatic polymer pellets of the invention can be prefoamed by using hot air or steam, in what are known as prefoamers, to give foam beads of density in the range from 20 to 100 kg/m3, in particular from 15 to 50 kg/m3, the final foaming step focusing a density preferably from 10 to 35 kg/m3. Eventually in order to reach the lower densities a second foaming step can be applied. After maturation, in a next step the foamed beads (to which a coating has been applied) are placed in molds where they are treated with steam and where they are further expanded and fused to give molded foams.
The molded foam is characterized by a thermal conductivity, in accordance to DIN 52612, of less than 36 mW/m·K for a foam density of 16 kg/m3 or lower, even of less than 34 mW/m·K for a foam density of 20 kg/m3 or lower, even of less than 31 mW/m·K for a foam density of 25 kg/m3 or lower.
The foam panels derived from the expandable vinyl aromatic polymers according to the present invention all have B2 rating (DIN 4102-1) and the average flame height, according to DIN 4102-1, below 10 cm and the single burning item (SBI) test according EN 13823 and classified according to EN 13501-1 at 20 kg/m3 density and 60 mm thickness of class B.
The following illustrative examples are merely meant to exemplify the present invention but they are not intended to limit or otherwise define the scope of the present invention.
All the examples comprise 6% by weight of athermanous particle, 0.15% by weight of high density polyethylene wax with a weight average molecular weight (Mw) of 2 kDa, 1.0% by weight of Emerald Innovation™ 3000 (Chemtura), 0.33% by weight, of 2,3-dimethyl-2,3-diphenylbutane (Curox® CC-DC from United Initiators)(synergist).
Examples 1 to 4 comprise 12.5% by weight, relative to Emerald Innovation™ 3000, of heat stabilizer wherein 100 parts of heat stabilizer 1 to 3 comprise 25 parts by weight of Ultranox 626, an organophosphate supplied by Addivant, 25 parts of Anox 20, a hindered phenolic supplied by Addivant and 50 parts of:
Example 5, comprises 6.75% by weight, relative to Emerald Innovation™ 3000, of heat stabilizer 1.
The foam panels derived from the expandable vinyl aromatic polymers according to the present invention all had B2 rating (DIN 4102).
In table 2 thermal conductivity (λ, in mW/m·K), determined in accordance to ISO 8301, is reported.
In tables 2 and 3, the test results of the Single Burning Item test, according to EN 13823, and classified according to EN 13501-1; are represented for foams 1 to 3, according to the invention and for the foams of comparative examples 4 and 5.
The values, as reproduced in tables 2 and 3, are the arithmetic mean of two measurement results which do not deviate by more than 10% from their arithmetic mean.
Foam panels 1 to 5 were subjected to the Single Burning Item test according to EN13823, for panels having a thickness of 60 mm, mounted and fixed according to EN 15715 and EN 13238. More precisely, the trial conditions are a panel thickness of 60 mm; a calcium silicate as a substrate; no air gap between the panels and the substrate; no air gap between the substrate and the backing board; the presence of horizontal and vertical joints; the use of mechanical fixation (standardized washer and screw).
Results are reported in tables 2 and 3, wherein:
Contrary to the foams of comparative examples 4 and 5, the foams derived from the expandable vinyl aromatic polymers according to the present invention, all answer the SBI class “B, s2, d0”.
Number | Date | Country | Kind |
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19195471.8 | Sep 2019 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2020/072594 | 8/12/2020 | WO |