DE102004058583A1 - Expandable styrene polymer granules and particle foams with reduced thermal conductivity - Google Patents

Abstract

Espanderable styrene polymer granules comprising DOLLAR A a) from 5 to 50% by weight of a filler selected from powdered inorganic substances such as talc, chalk, kaolin, aluminum hydroxide, aluminum nitrite, aluminum silicate, barium sulfate, calcium carbonate, titanium dioxide, calcium sulfate, silica, quartz powder, Aerosil , Alumina or wollastonite and DOLLAR A b) contain 0.1 to 10 wt .-% of carbon black or graphite DOLLAR A, as well as processes for their preparation and obtainable therefrom particle foams with reduced thermal conductivity.

Description

• a) 5 bis 50 Gew.-% eines Füllstoffes, ausgewählt aus pulverförmigen anorganische Stoffen, wie Talk, Kreide, Kaolin, Aluminiumhydroxid, Aluminiumnitrit, Aluminiumsilikat, Bariumsulfat, Calciumcarbonat, Titandioxid, Kreide, Calciumsulfat, Kaolin, Kieselsäure, Quarzmehl, Aerosil, Tonerde oder Wollastonit und
• b) 0,1 bis 10 Gew.-% Ruß oder Graphit enthalten, sowie Verfahren zu deren Herstellung und daraus erhältliche Partikelschaumstoffe mit verminderter Wärmeleitfähigkeit.

The invention relates to expandable styrene polymer granules which

• a) 5 to 50 wt .-% of a filler selected from powdery inorganic materials such as talc, chalk, kaolin, aluminum hydroxide, aluminum nitrite, aluminum silicate, barium sulfate, calcium carbonate, titanium dioxide, chalk, calcium sulfate, kaolin, silica, quartz, Aerosil, alumina or wollastonite and
• b) 0.1 to 10 wt .-% carbon black or graphite, and to processes for their preparation and obtainable therefrom particle foams with reduced thermal conductivity.

It is known to reduce the thermal conductivity of polystyrene foams athermane materials such as carbon black (EP-A 372 343) or graphite (EP-A 981 574). Here are each by nature and incorporation high levels of athermanous materials needed due to the nucleating effect to problems in the homogeneous To be trained can. Furthermore you can the mechanical properties of the foams produced therefrom and whose fire behavior is negatively influenced.

method for the production of flame-retardant, expandable styrene polymers by extrusion of a blowing agent-containing Styrene polymer melt are z. B from EP-A 0 981 574 and WO 97/45477 known. Here are halogenated flame retardants, such as Hexabromcyclododekan (HBCD) optionally together with other additives, e.g. flame retardant synergists, such as dicumyl peroxide or dicumyl, melted with polystyrene and subsequently added a propellant.

task The present invention was therefore, the disadvantages mentioned remedy and self-extinguishing Styrene polymer particle foams with low thermal conductivity as well as a method of making expandable Styrene polymers obtained by prefoaming and sintering with hot air or Water vapor to self-extinguishing Styrene polymer particle foams are processable.

Accordingly, were found the expandable styrene polymer granules described above.

Prefers becomes the soot or Graphite in amounts of 2 to 8 wt .-% used.

Carbon black with an average primary particle size in the range from 10 to 300 nm, in particular in the range from 30 to 200 nm, is preferably used. The BET surface area is preferably in the range of 10 to 120 m ² / g.

When Graphite is preferably graphite having a mean particle size in the range from 1 to 50 μm used.

Especially preferably contains EPS granules as flame retardants hexabromocyclododecane (HBCD) and as flame retardant synergist dicumyl or dicumyl peroxide.

The weight ratio from flame retardant synergist to organic bromine compound is in usually in the range of 1 to 20, preferably in the range of 2 to 5th

Of further were particle foam moldings, available through weld together of prefoamed Foam particles of expandable, filler-containing, thermoplastic Polymer granules, found, wherein the particle foam a Density in the range of 8 to 200 g / l, preferably in the range of 10 to 50 g / l.

Surprisingly show the particle foam moldings according to the invention despite the presence of fillers a high closed-cell density, usually more than 60%, preferably more than 70, more preferably more than 80% of the cells the individual foam particles are closed-celled.

Suitable fillers are organic and inorganic powders or fibrous materials, as well as mixtures thereof. As organic fillers z. As wood flour, starch, flax, hemp, ramie, jute, sisal-cotton cellulose or aramid fibers are used. As inorganic fillers z. B. Carbona te, silicates, barite, glass beads, zeolites or metal oxides are used. Preference is given to pulverulent inorganic substances such as talc, chalk, kaolin (Al ₂ (Si ₂ O ₅ ) (OH) ₄ ), aluminum hydroxide, magnesium hydroxide, aluminum nitrite, aluminum silicate, barium sulfate, calcium carbonate, calcium sulfate, silica, quartz powder, Aerosil, alumina or wollastonite or spherical or fibrous inorganic materials such as glass beads, glass fibers or carbon fibers.

The average particle diameter or in the case of fibrous fillers the length should in the range of cell size or lie smaller. Preference is given to an average particle diameter in the range of 1 to 100 μm, preferred in the range of 2 to 50 μm.

Particular preference is given to inorganic fillers having a density in the range from 2.0 to 4.0 g / cm ³ , in particular in the range from 2.5 to 3.0 g / cm ³ . The whiteness / brightness (DIN / ISO) is preferably 50 to 100%, in particular 70 to 98%.

The oil number after ISO 787/5 of preferred fillers is in the range of 2 to 200 g / 100 g, especially in the range from 5 to 150g / 100g.

By the type and amount of fillers can the properties of the expandable thermoplastic polymers and the one available from it Influence particle foam moldings. The proportion of the filler is usually in the range of 1 to 50, preferably 5 to 30 wt .-%, based on the thermoplastic polymer. At filler contents in the range from 5 to 15% by weight will not significantly deteriorate mechanical properties of the particle foams, such as flexural strength or compressive strength observed. Through the use of adhesion promoters, such as maleic anhydride-modified Styrene copolymers, epoxy group-containing polymers, organosilanes or Styrenic copolymers with isocyanate or acid groups may interfacial of the filler to the polymer matrix and thus the mechanical properties of the Particle foam moldings are significantly improved.

In In general, inorganic fillers reduce flammability. In particular, by the addition of inorganic powders, such as aluminum hydroxide the fire behavior can be significantly improved.

Surprisingly show the thermoplastic according to the invention Polymer granules even at high Füllstoffgehalten a small Propellant loss during storage. Due to the nucleating Effect is also related to a reduction of the blowing agent content on the polymer, possible.

When thermoplastic polymers can For example, styrene polymers, polyamides (PA), polyolefins, such as Polypropylene (PP), polyethylene (PE) or polyethylene-propylene copolymers, Polyacrylates, such as polymethyl methacrylate (PMMA), polycarbonate (PC), Polyester, such as polyethylene terephthalate (PET) or polybutylene terephthalate (PBT), polyethersulfones (PES), polyetherketones or polyethersulfides (PES) or mixtures thereof. Especially preferred styrene polymers are used.

It has been found that styrene polymers with molecular weights M _w of less than 160,000 lead to polymer abrasion during granulation. Preferably, the expandable styrene polymer has a molecular weight in the range of 190,000 to 400,000 g / mol, more preferably in the range of 220,000 to 300,000 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.

In order to obtain the smallest possible granulate particles, the strand expansion after the nozzle exit should be as low as possible. It has been shown that the strand expansion can be influenced inter alia by the molecular weight distribution of the styrene polymer. The expandable styrene polymer should therefore preferably have a molecular weight distribution with a nonuniformity M _w / M _n of at most 3.5, more preferably in the range of 1.5 to 2.8, and most preferably in the range of 1.8 to 2.6.

Prefers are used as styrene polymers crystal clear polystyrene (GPPS), impact polystyrene (HIPS), anionically polymerized polystyrene or impact polystyrene (A-IPS), styrene-a-methstyrene 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).

The styrene polymers mentioned can be used to improve the mechanical properties or the Temperature resistance optionally 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 wt .-%, preferably in the range of 1 to 10 wt .-%, based on the polymer melt to be 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 or biodegradable aliphatic or aliphatic / aromatic copolyesters possible.

When compatibilizers are suitable e.g. Maleic anhydride-modified Styrene copolymers, polymers containing epoxy groups or organosilanes.

Of the Styrene polymer melt can also polymer recyclates of said thermoplastic polymers, in particular styrene polymers and expandable styrene polymers (EPS) in amounts which are not essential to their properties deteriorate, usually in amounts of at most 50 wt .-%, in particular in amounts of 1 to 20 wt .-%.

The propellant-containing styrene polymer melt usually contains one or more Propellants in homogeneous distribution in a proportion of total 2 to 10 wt .-%, preferably 3 to 7 wt .-%, based on the propellant-containing Styrolpolyermschmelze. As propellants, the customary ones physical blowing agents used in EPS, such as aliphatic Hydrocarbons having 2 to 7 carbon atoms, alcohols, ketones, Ethers or halogenated hydrocarbons. Preference is given to isobutane, n-butane, iso-pentane, n-pentane used.

to Improvement of foamability can finely distributed inner water droplets be introduced into the Styrolpolymermatirx. This can be, for example by the addition of water into the molten styrene polymer matrix respectively. The addition of the water can be done locally before, with or after the Treibmitteldosierung done. A homogeneous distribution of water can be achieved by means of dynamic or static mixers.

In As a rule, 0 to 2, preferably 0.05 to 1.5 wt .-% water, based to the styrene polymer, sufficient.

expandable Styrene polymers (EPS) with at least 90% of the internal water in the form of inner water droplets with a diameter in the range of 0.5 to 15 microns form foams during foaming sufficient cell count and homogeneous foam structure.

The added amount of blowing agent and water is chosen so that the expandable styrene polymers (EPS) defines an expansion capacity α as bulk density before foaming / bulk density after foaming at the most 125 preferably have 25 to 100.

The expandable according to the invention Styrenic polymer granules (EPS) generally have a bulk density from at most 700 g / l preferably in the range of 590 to 660 g / l. Using of fillers can dependent on on the type and amount of filler bulk densities in the range of 590 to 1200 g / l occur.

Of others can the styrene polymer melt in addition to the fillers Additives, nucleating agents, plasticisers, flame retardants, soluble and insoluble inorganic and / or organic dyes and pigments, e.g. IR absorber, like soot, Graphite or aluminum powder together or spatially separated, e.g. over mixer or side extruders are added. In general, the dyes and pigments in amounts ranging from 0.01 to 30, preferably in the Range of 1 to 5 wt .-% added. For homogeneous and microdispersed Distribution of the pigments in the styrenic polymer may be particularly be useful in polar pigments a dispersing aid, e.g. organosilanes, epoxy group containing Polymers or maleic anhydride-grafted Styrene polymers to use. Preferred plasticizers are mineral oils, low molecular weight Styrene polymers, phthalates, in amounts of 0.05 to 10 wt .-%, based on the Styrene polymer can be used.

• a) Polymerisationsreaktor-statischer Mischer/Kühler-Granulator
• b) Polymerisationsreaktor-Extruder-Granulator
• c) Extruder-statischer Mischer-Granulator
• d) Extruder-Granulator

To prepare the expandable styrene polymers according to the invention, the blowing agent is mixed into the polymer melt. The process comprises the stages a) melt production, b) mixing c) cooling d) conveying and e) granulating. Each of these stages can be carried out by the apparatuses or apparatus combinations known in plastics processing. For mixing, static or dynamic mixers are suitable, for example extruders. The polymer melt can be taken directly from a polymerization reactor or produced directly in the mixing extruder or a separate melt extruder by melting polymer granules. The cooling of the melt can be done in the mixing units or in separate coolers. For example, pressurized underwater granulation, granulation with rotating knives and cooling by spray misting of tempering liquids or sputtering granulation may be considered for the granulation. For carrying out the method suitable apparatus arrangements are for. B .:

• a) Polymerization Reactor Static Mixer / Cooler Granulator
• b) Polymerization Reactor Extruder Granulator
• c) extruder-static mixer-granulator
• d) extruder granulator

Farther the arrangement can side extruder for the introduction of additives, e.g. of solids or thermally sensitive additives exhibit.

The propellant-containing styrene polymer melt is usually with a Temperature in the range of 140 to 300 ° C, preferably in the range of 160 to 240 ° C through the nozzle plate promoted. A cool down up to the range of the glass transition temperature is not necessary.

The nozzle plate is at least at the temperature of the blowing agent-containing polystyrene melt heated. Preferably, the temperature of the nozzle plate is in the range of 20 up to 100 ° C above the Temperature of the blowing agent-containing polystyrene melt. This will be Polymer deposits in the nozzles prevented and a trouble-free Granulation guaranteed.

Around marketable To obtain granule sizes should be the diameter (D) of the nozzle holes at the nozzle exit in the range of 0.2 to 1.5 mm, preferably in the range of 0.3 to 1.2 mm, more preferably in the range of 0.3 to 0.8 mm. This allows granule sizes to be absorbed even after strand expansion 2 mm, especially in the range 0.4 to 1.4 mm targeted.

The Strand expansion can except on the Molecular weight distribution can be influenced by the nozzle geometry. The nozzle plate preferably has holes with a ratio L / D of at least 2, being the length (L) the nozzle area, its diameter at most the diameter (D) at the nozzle outlet corresponds, designated. Preferably, the ratio L / D is in the range of 3-20.

in the Generally, the diameter (E) of the holes should be at the nozzle inlet the nozzle plate at least twice as big as the diameter (D) at the nozzle outlet be.

A embodiment the nozzle plate has holes with conical inlet and an inlet angle α smaller 180 °, preferably in the range of 30 to 120 °. In a further embodiment owns the nozzle plate Holes with conical outlet and a discharge angle β smaller 90 °, preferably in the range of 15 to 45 °. For targeted granule size distributions To produce the styrene polymer, the nozzle plate with holes of different Outlet diameter (D) equipped become. The different embodiments the nozzle geometry can also be combined with each other.

• a) Polymerisation von Styrolmonomer und gegebenenfalls copolymersierbaren Monomeren,
• b) Entgasungung der erhaltenen Styrolpolymerschmelze,
• c) Einmischen des Treibmittels und gegebenenfalls Additiven, in die Styrolpolymerschmelze mittels statischen oder dynamischen Mischer bei einer Temperatur von mindestens 150°C, bevorzugt 180–260°C,
• d) Kühlen der treibmittelhaltigen Styrolpolymerschmelze auf eine Temperatur, die mindestens 120°C, bevorzugt 150–200°C beträgt,
• e) Zugabe des Füllstoffs,
• f) Austrag durch eine Düsenplatte mit Bohrungen, deren Durchmesser am Düsenaustritt höchstens 1,5 mm beträgt und
• g) Granulieren der treibmittelhaltigen Schmelze.

A particularly preferred process for preparing expandable styrenic polymers comprises the steps

• a) polymerization of styrene monomer and optionally copolymerizable monomers,
• b) degassing the resulting styrene polymer melt,
• c) incorporating the blowing agent and optionally additives into the styrene polymer melt by means of a static or dynamic mixer at a temperature of at least 150 ° C., preferably 180-260 ° C.,
• d) cooling the propellant-containing styrene polymer melt to a temperature which is at least 120 ° C., preferably 150-200 ° C.,
• e) adding the filler,
• f) discharge through a nozzle plate with holes whose diameter at the nozzle outlet is at most 1.5 mm and
• g) granulating the blowing agent-containing melt.

In step g), the granulation directly behind the nozzle plate under water at a pressure in Be rich from 1 to 25 bar, preferably 5 to 15 bar.

by virtue of the polymerization in step a) and degassing in step b) is for the propellant impregnation in step c) directly a polymer melt available and a melting of Styrene polymers is not necessary. This is not only more economical, but leads also to expandable styrene polymers (EPS) with low Sty rolmonomergehalten, since the mechanical shear effect in the melting area of an extruder, which usually leads to a split-off of monomers, is avoided. To keep the styrene monomer content low, especially below 500 ppm with Styrolmomomergehalten, it is also appropriate to the mechanical and thermal energy input in all subsequent process steps as low as possible to keep. Therefore, shear rates below 50 / sec are particularly preferred, preferably 5 to 30 / sec, and temperatures below 260 ° C and short Residence times in the range of 1 to 20, preferably 2 to 10 minutes complied with in steps c) to e). Particularly preferred exclusively static mixers and static coolers throughout the process used. The polymer melt can by pressure pumps, z. B. gear pumps promoted and be discharged.

A another possibility for reducing styrene monomer content and / or residual solvents such as Ethylbenzene is in step b) high degassing means Entrainers, such as water, nitrogen or carbon dioxide, or to carry out the polymerization step a) anionically. The Anionic polymerization of styrene not only leads to styrenic polymers with low Styrolmonomeranteil, but at the same time to the low Styrene oligomer.

to Improving processability can make the finished expandable Styrene polymer granules by glycerol esters, antistatic agents or anticaking agents to coat.

The expandable according to the invention Styrenic polymer granules (EPS) have a function of filler type and content usually higher bulk densities generally ranging from 590 to 1200 g / l.

The expandable according to the invention thermoplastic polymer granules show even at low propellant contents a good capacity for expansion. The bond is significantly lower even without coating at conventional EPS beads.

fillers with particle sizes in the range from 0.1 to 100 μm, in particular in the range of 0.5 and 10 microns in the polystyrene foam particles at levels of 10 wt .-%, a reduction in thermal conductivity by 1 to 3 mW. Therefore Already at lower levels and IR absorbers, such as carbon black and graphite comparatively low thermal conductivities to reach.

Prefers is used to reduce the thermal conductivity an IR absorber such as soot or Graphite in amounts of 0.1 to 10 wt .-%, in particular in amounts used from 2 to 8 wt .-%.

When using smaller amounts of fillers, eg. B. under 5 wt .-%, it is also possible to use carbon black in amounts of 1 to 25 wt .-%, preferably in the range of 10 to 20 wt .-%. At these high carbon black contents, the carbon black addition is preferably mixed into the styrene polymer melt via the main stream and a side stream extruder. The addition via extruder allows a simple comminution of the carbon black agglomerates to an average agglomerate size in the range of 0.3 to 10 .mu.m, preferably in the range of 0.5 to 5 .mu.m, and homogeneous dyeing of the expandable styrene polymer granules which form closed-cell foam particles having a density in the range of 5-40 kg / m ³ , in particular 10-15 kg / m ³ can be foamed. The particle foams obtainable with 10 to 20% by weight of carbon black after foaming and sintering achieve a thermal conductivity λ, determined at 10 ° C. to DIN 52612, in the range from 30 to 33 mW / mK.

Carbon black with an average primary particle size in the range from 10 to 300 nm, in particular in the range from 30 to 200 nm, is preferably used. The BET surface area is preferably in the range of 10 to 120 m ² / g.

When Graphite is preferably graphite having a mean particle size in the range from 1 to 50 μm used.

• a) Einmischen (i) eines organischen Treibmittels, (ii) 5–50 Gew.-%, bezogen auf das Styolpolymerisat, eines Füllstoffes, ausgewählt aus pulverförmigen anorganische Stoffen, wie Talk, Kreide, Kaolin, Aluminiumhydroxid, Aluminiumnitrit, Aluminiumsilikat, Bariumsulfat, Calciumcarbonat, Titandioxid, Calciumsulfat, Kieselsäure, Quarzmehl, Areosil, Tonerde oder Wollastonit und (iii) 0,1 bis 10 Gew.-%, bezogen auf das Styolpolymerisat, Ruß oder Graphit in die Styrolpolmerisatschmelze mittels statischen oder dynamischen Mischer bei einer Temperatur von mindestens 150°C,
• b) Kühlen der treibmittel- und Füllstoff-haltigen Polymerschmelze auf eine Temperatur von mindestens 120°C
• c) Austrag durch eine Düsenplatte mit Bohrungen, deren Durchmesser am Düsenaustritt höchstens 1,5 mm beträgt und
• d) Granulieren der treibmittelhaltigen Schmelze direkt hinter der Düsenplatte unter Wasser bei einem Druck im Bereich von 1 bis 20 bar.

A preferred process for preparing expandable styrene polymers comprises the steps

• a) mixing in (i) an organic blowing agent, (ii) 5-50% by weight, based on the styol polymer, of a filler selected from pulverulent inorganic substances, such as talc, chalk, kaolin, aluminum hydroxide, aluminum nitrite, aluminum silicate, barium sulfate, Calcium carbonate, titanium dioxide, calcium sulfate, silicic acid, quartz flour, areosil, alumina or wollastonite and (iii) from 0.1 to 10% by weight, based on the styol polymer, of carbon black or graphite in the styrene polymer melt, by means of a static or dynamic mixer at a temperature of at least 150 ° C,
• b) cooling the propellant and filler-containing polymer melt to a temperature of at least 120 ° C.
• c) discharge through a nozzle plate with holes whose diameter at the nozzle outlet is at most 1.5 mm and
• d) granulating the blowing agent-containing melt directly behind the nozzle plate under water at a pressure in the range of 1 to 20 bar.

The inventive expandable styrene polymer granules can by means of hot air or steam to give foam particles having a density in the range from 8 to 200 kg / m ^3, preferably in the range of 10 to 50 kg / m ³ prefoamed and then welded together in a closed mold to foam moldings.

In a polystyrene melt of PS 158 K BASF Aktiengesellschaft with a viscosity number VZ of 98 ml / g (M _w = 280,000 g / mol, nonuniformity M _w / M _n = 2.8) in an extruder 7 wt .-%, based on polystyrene, pentane mixed. After cooling the propellant-containing melt from originally 260 ° C to a temperature of 190 ° C, a mixture of polystyrene melt, filler (chalk, Ulmer white (Omya)), IR absorber (carbon black or graphite, UF298 Kropfmühl) and Flame retardant (HBCD) according to Table 1 was added and mixed into the main stream. In addition, at the level of the side-type extruder via a metering lance, the pentane-dissolved flame retardant synergists dicumyl (DC) or dicumyl peroxide are metered into the cooled main stream by means of a piston pump. The mixture of polystyrene melt, blowing agent, flame retardant and synergist was at 60 kg / h through a nozzle plate with 32 holes (diameter of the nozzle 0.75 mm) promoted. With the help of pressurized underwater granulation, compact granules with a narrow size distribution were produced.

These Granules were in flowing Steam to foam beads (20 g / l) prefoamed, 24 Stored for hours and then in gas-tight forms with Water vapor to foam bodies welded.

The Thermal conductivity λ was determined at 10 ° C according to DIN 52612. Afterburning times of less than 6 seconds are suitable to pass the B2 test according to DIN 4102.

Table 1:

Claims (6)

Expandable styrene polymer granules containing a) 5 to 50 wt .-% of a filler selected from powdery inorganic materials such as talc, chalk, kaolin, aluminum hydroxide, aluminum nitrite, aluminum silicate, barium sulfate, calcium carbonate, titanium dioxide, calcium sulfate, silica, quartz, Aerosil, alumina or wollastonite and b ) 0.1 to 10% by weight of carbon black or graphite. Expandable styrene polymer granules according to claim 1, characterized in that it contains 0.2 to 5 wt .-% of an organic Bromine compound having a bromine content of at least 70% by weight as Flame retardants included. Expandable styrene polymer granules according to claim 2, characterized in that it contains 0.05 to 1.0 wt .-% dicumyl or dicumyl peroxide as a flame retardant synergist. Expandable styrene polymer granules according to one of claims 1 to 3, characterized in that they contain 3 to 7 wt .-% of an organic Propellant included. Process for producing expandable styrenic polymer granules, comprising the steps a) meddle (i) an organic Propellant, (ii) 5-50 Wt .-%, based on the styol polymer, of a filler, selected from powdery inorganic substances such as talc, chalk, kaolin, aluminum hydroxide, Aluminum nitrite, aluminum silicate, barium sulfate, calcium carbonate, Titanium dioxide, calcium sulfate, silicic acid, quartz flour, areosil, alumina or wollastonite and (iii) 0.1 to 10% by weight, based on the Styol polymer, carbon black or Graphite in the Styrolpolmerschmelze by static or dynamic Mixer at a temperature of at least 150 ° C, b) cooling the blowing agent and filler-containing Polymer melt to a temperature of at least 120 ° C, c) Discharge through a nozzle plate with holes whose diameter at the nozzle exit at most 1.5 mm and d) granulating the blowing agent-containing melt directly behind the nozzle plate under water at a pressure in the range of 1 to 20 bar. Process for producing particle foam moldings, characterized in that expandable, styrene polymer granules according to claim 1 in a first step by means of hot air or water vapor to foam particles prefoamed at a density in the range of 8 to 200 g / l and welded in a second step in a closed mold.