US20060058407A1

US20060058407A1 - Expandable vinylaromatic polymers and process for their preparation

Info

Publication number: US20060058407A1
Application number: US11/250,365
Authority: US
Inventors: Dario Ghidoni; Roberto Lanfredi; Gilberto Frigerio; Alessandro Casalini
Original assignee: Polimeri Europa SpA
Current assignee: Versalis SpA
Priority date: 2001-10-18
Filing date: 2005-10-17
Publication date: 2006-03-16
Also published as: CA2462137A1; DE60211545D1; DE60211545T2; JP2005506424A; CA2462137C; MXPA04003518A; RU2004105595A; PL368372A1; US20040242713A1; CN1561360A; WO2003035728A1; EP1448681A1; EP1448681B1; ITMI20012168A1; BR0212954A; JP4157475B2; BR0212954B1; ES2265066T3; RU2283323C2; US7279504B2

Abstract

Expandable vinylaromatic polymers which comprise: a) a matrix obtained by polymerizing 50-100% by weight of one or more vinylaromatic monomers and 0.50% by weight of a copolymerizable monomer; b) 1-10% by weight, calculated with respect to the polymer (a), of an expanding agent englobed in the polymeric matrix; c) 0.05-25% by weight, calculated with respect to the polymer (a), of an inorganic filler homogeneously distributed in the polymeric matrix with a substantially spherical granulometry, an average diameter ranging from 0.01 to 100 μm, a refraction index higher than 1.6 and a white index, as defined in “Colour Index” (third edition published by the Society of Dyers and Colourists, 1982), equal to or lower than 22.

Description

The present invention relates to expandable vinylaromatic polymers and the process for their preparation.
More specifically, the present invention relates to a process for the preparation of expandable vinylaromatic polymers which, after expansion, have a reduced thermal conductivity also with a low density and to the products thus obtained.
Expandable vinylaromatic polymers, and among these expandable polystyrene in particular, are known products which have been used for a long time in various applicative sectors, among which one of the most important is the field of thermal insulation.
These expanded products are obtained by swelling in a closed mould beads of expanded polymer impregnated with a gas and molding the swollen particles contained inside the mould by means of the contemporaneous effect of pressure and temperature. The swelling of the particles is generally effected with vapour, or another gas, maintained at a temperature slightly higher than the glass transition temperature (Tg) of the polymer.
A particular applicative field of expanded polystyrene is that of thermal insulation in the building industry where it is generally used in the form of flat sheets. The flat expanded polystyrene sheets are usually used with a density of about 30 g/l as the thermal conductivity of the polymer shows a minimum at these values. It is not advantageous to fall below this density limit, even if it is technically possible, as it causes a drastic increase in the thermal conductivity of the sheet which must be compensated by an increase in its thickness.
U.S. Pat. No. 6,130,265 describes a method for preparing particles of expandable polystyrene which allows thermoinsulating sheets to be prepared for the building industry, having a density lower than 30 g/l but with a thermal conductivity analogous to that of traditional sheets. According to this method, particles of expandable polystyrene can be prepared, which are capable of giving articles, for example, sheets, with a density ranging from 10 to 15 g/l and a thermal conductivity which is such as to satisfy the request of class 035 of the DIN 18164, Part 1, Standard englobing in the particle itself from 0.05 to 25% by weight of graphite powder in the form of substantially spherical particles with an average diameter ranging from 0.1 to 50 μm. More specifically, the method of the U.S. patent cited above comprises polymerizing the styrene monomer, or a solution of polystyrene in styrene, in an aqueous suspension, in the presence of graphite particles and conventional reagents and/or polymerization additives. Expandable polystyrene spherical beads are thus obtained with an average diameter ranging from 0.2 to 2 mm in which the graphite in powder form is homogeneously distributed.
The Applicant has now found that it is possible to obtain expandable styrene polymers capable of providing low density expanded materials, with characteristics comparable to those of the materials obtained with the method of the known art, without having to resort to the use of an athermanous additive such as graphite which has, among other things, the defect of giving the polymer, before and after expansion, an unaesthetic grey colour, sometimes intense. It has been found, in fact, that it is possible to obtain products based on vinylaromatic polymers with a density much lower than 30 g/l and with a thermal conductivity also capable of satisfying class 035 of the DIN 18164 Part 1, Standard by substituting athermanous graphite, i.e. capable of absorbing infrared radiation, with materials having a refraction index which is sufficiently higher than that of the polymer and which are therefore capable of favouring the reflection of infrared radiation. This result is particularly interesting as it also allows a material such as titanium dioxide to be selected, which, as it is white, does not alter the colouring of the polymer, in particular polystyrene.
An object of the present invention therefore relates to expandable vinylaromatic polymers which comprise:

a) a matrix obtained by polymerizing 50-100% by weight of one or more vinylaromatic monomers and 0.50% by weight of a copolymerizable monomer;
b) 1-10% by weight, calculated with respect to the polymer (a), of an expanding agent englobed in the polymeric matrix;
c) 0.05-25% by weight, calculated with respect to the polymer (a), of an inorganic filler homogeneously distributed in the polymeric matrix with a substantially spherical granulometry, an average diameter ranging from 0.01 to 100 μm, a refraction index higher than 1.6 and a white index, as defined in “Colour Index” (third edition published by The Society of Dyers and Colourists, 1982), equal to or lower than 22.

The term “vinylaromatic monomer”, as used in the present description and claims, essentially refers to a product which corresponds to the following general formula:

wherein R is a hydrogen or a methyl group, n is zero or an integer ranging from 1 to 5 and Y is a halogen, such as chlorine or bromine, or an alkyl or alkoxyl radical having from 1 to 4 carbon atoms.
Examples of vinylaromatic monomers having the general formula defined above are: styrene, α-methylstyrene, methylstyrene, ethylstyrene, butylstyrene, dimethylstyrene, mono-, di-, tri-, tetra- and penta-chlorostyrene, bromo-styrene, methoxy-styrene, acetoxy-styrene, etc. Preferred vinylaromatic monomers are styrene and α-methylstyrene.
The vinylaromatic monomers having general formula (I) can be used alone or in a mixture of up to 50% by weight with other copolymerizable monomers. Examples of these monomers are (meth)acrylic acid, C₁-C₄alkyl esters of (meth)acrylic acid, such as methyl acrylate, methylmethacrylate, ethyl acrylate, ethylmethacrylate, isopropyl acrylate, butyl acrylate, amides and nitriles of (meth)acrylic acid such as acrylamide, methacrylamide, acrylonitrile, methacrylonitrile, butadiene, ethylene, divinylbenzene, maleic anhydride, etc. Preferred copolymerizable monomers are acrylonitrile and methylmethacrylate.
Any expanding agent capable of being englobed in the vinylaromatic polymeric matrix, can be used in a combination with the vinylaromatic polymers object of the present invention. Typical examples are aliphatic hydrocarbons, freon, carbon dioxide, water, etc.
The inorganic filler with a refraction index higher than 1.6, preferably from 1.6 to 3, extremes included, and with a white index equal to or lower than 22, preferably between 21 and 5, extremes included, can be added to the vinylaromatic polymer both by polymerization in suspension and by means of the continuous mass technique, in such quantities as to give a final concentration in the polymer ranging from 0.05-25% by weight, preferably from 0.5 to 8%. The granulometry of the filler preferably ranges from 0.1 to 50 μm. The preferred inorganic filler is represented by titanium dioxide and barium sulfate.
At the end of the addition of the filler, an expandable polymer is obtained, which can be transformed to produce expanded articles having a density ranging from 5 to 50 g/l, preferably from 10 to 25 g/l. These materials also have an excellent thermal insulation capacity expressed by a thermal conductivity ranging from 25 to 50 mW/mK, preferably from 30 to 45 mW/mK which is generally on an average even over 10% lower than that of equivalent non-filled expanded materials currently on the market, for example EXTIR A-5000 of EniChem S.p.A., as illustrated in Tables 1 and 2 enclosed. Thanks to these characteristics of the expandable polymers object of the present invention, it is possible to prepare thermo-insulating articles with significant material savings or, for example, to prepare sheets having a lesser thickness than those produced with traditional nonfilled polymers, with a consequent reduction in space.
Conventional additives, generally used with traditional materials, such as pigments, stabilizers, flame-retardants, antistatic agents, detaching agents, etc. can be added to the expandable polymers object of the present invention.
A further object of the present invention relates to the processes for the preparation of expandable polymers with an improved thermal conductivity, after expansion, with a density lower than 30 g/l.
In particular, a further object of the present invention relates to a process for preparing expandable vinylaromatic polymers which comprises polymerizing in aqueous suspension one or more vinylaromatic monomers, optionally together with at least one polymerizable comonomer in a quantity of up to 50% by weight, in the presence of an inorganic filler with a substantially spherical granulometry, an average diameter ranging from 0.01 to 100 μm, a re-fraction index higher than 1.6 and a white index, as defined in “Colour Index” (third edition published by The Society of Dyers and Colourists, 1982), equal to or lower than 22, and an expanding agent added before, during or after the end of the polymerization.
At the end of the polymerization, substantially spherical polymer beads are obtained, with an average diameter ranging from 0.2 to 2 mm, inside which the inorganic additive is homogeneously dispersed.
During the polymerization in suspension, polymerization additives, typically used for producing expandable vinylaromatic polymers, are adopted, such as peroxide initiators, stabilizing agents of the suspension, chain transfer agents, expanding aids, nucleating agents, plasticizers, etc. In particular, it is preferable to add flame-retardant agents during the polymerization, in a quantity ranging from 0.1% to 8% by weight, with respect to the weight of the resulting polymer. Flame-retardant agents particularly suitable for the expandable vinylaromatic polymers, object of the present invention, are brominated aliphatic, cycloaliphatic, aromatic compounds such as hexabromocyclododecane, pentabromomonochlorocyclohexane and pentabromophenyl allyl ether.
The expanding agents are preferably added during the polymerization phase and are selected from aliphatic or cycloaliphatic hydrocarbons containing from 3 to 6 carbon atoms such as n-pentane, isopentane, cyclopentane or their mixtures; the halogenated derivatives of aliphatic hydrocarbons containing from 1 to 3 carbon atoms such as, for example, dichlorodifluoromethane, 1,2,2-trifluoroethane, 1,1,2-trifluoroethane; carbon dioxide and water.
To improve the stability of the suspension, it is possible to use a solution of vinylaromatic polymer in the monomer, or mixture of monomers, in which the concentration of polymer ranges from 1 to 30% by weight, preferably from 5 to 20%. The solution can be obtained either by dissolving a preformed polymer (for example fresh polymer or the waste products of previous polymerizations and/or expansions) in the monomer or by pre-polymerizing the monomer, or mixture of monomers, in mass, in order to obtain the above concentrations, and then continuing the polymerization in aqueous suspension in the presence of the remaining additives.
Another object of the present invention relates to a process for preparing in mass and in continuous, expandable vinylaromatic polymers, which comprises the following steps in series:

i. feeding a vinylaromatic polymer, as described above, to an extruder, together with an inorganic filler, having a substantially spherical granulometry, an average diameter ranging from 0.01 to 100 μm, a refraction index higher than 1.6 and a white index, as defined in “Colour Index” (third edition published by The Society of Dyers and Colourists, 1982), equal to or lower than 22;
ii. heating the vinylaromatic polymer to a temperature higher than the relative melting point;
iii. injecting the expanding agent and possible additives such as flame-retardant agents, into the molten polymer before extrusion through a die; and
iv. forming expandable beads, through a die, in a substantially spherical form with an average diameter ranging from 0.2 to 2 mm.

A detailed method for preparing vinylaromatic polymers in mass and in continuous is provided in European patent EP 126,459.
At the end of the polymerization, either it be carried out in suspension or in continuous mass, the expandable beads produced are subjected to pre-treatment generally applied to conventional expandable beads and which essentially consists in:

1. coating the beads with a liquid antistatic agent such as amines, tertiary ethoxylated alkylamines, ethylene oxide-propylene oxide copolymers, etc. The purpose of this agent is to facilitate both the adhesion of the “coating” and also the screening of the beads prepared in suspension;
2. applying the “coating” to the above beads, said coating essentially consisting of a mixture of mono-, di- and tri-esters of glycerin (or other alcohols) with fatty acids and of metallic stearates such as zinc and/or magnesium stearate.

Alternatively, the inorganic filler can also be added in the coating, together with the mixture of esters.
Some illustrative but non-limiting examples are provided for a better understanding of the present invention and for its embodiment.

EXAMPLE 1

A mixture of 150 parts by weight of water, 0.1 parts of sodium pyrophosphate, 100 parts of styrene, 0.15 parts of benzoyl peroxide, 0.25 parts of ter-butyl perbenzoate and 1 part of titanium dioxide with a substantially spherical granulometry and an average diameter of about 0.2 μm, are charged into a closed, stirred container. The mixture is heated to 90° C. under stirring.
After about 2 hours at 90° C., 4 parts of a solution at 10% of polyvinylpyrrolidone are added. The mixture is heated, under stirring, for a further 2 hours to 100° C., 7 parts of a 70/30 mixture of n-pentane and i-pentane are added and the mixture heated for a further 4 hours to 125° C.
The beads of expandable polymer thus produced are subsequently recovered, washed with deionized water, dried in a stream of warm air, added with 0.02% of ethoxylated amine, and screened by separating the fraction with a diameter ranging from 1 to 1.5 mm.
0.2% of glycerylmonosterate and 0.05% of magnesium stearate are then added to the fraction.
The product is pre-expanded with vapour at a temperature of 100° C. for three contact times and aged for a day (density in Table 1).
A part of the beads is expanded a second time to reach even lower densities.
Both the beads expanded once only and those expanded twice were used for the moulding of blocks (dimensions 1040×1030×550 mm) at a pressure of 0.4 bars, and the cooling time was measured (data in Table 2—sheet 1).
The blocks were then evaluated (shrinkage, or the difference between the volume of the block and the volume of the mould) and cut to prepare flat sheets for measuring the sintering and thermal conductivity. The thermal conductivity was 36.7 mW/mK whereas that of a sheet having the same density prepared with a traditional non-filled reference product (EXTIR A-5000), was 42.5 mW/mK.
Table 2 indicates the physical characteristics of an expanded polystyrene block obtained with the expandable beads, object of the present invention, in a first and second expansion and compared with an analogous block obtained from the commercial reference product. The block obtained with the beads object of the present invention surprisingly shows a drastic increase in the sintering degree.

EXAMPLE 2

A polystyrene having a Melt Index of 10 g/10′ at 200° C./5 kg premixed with titanium dioxide alone (2 and 4%) in a first phase, and with barium sulfate alone (2%) in a second phase, is fed into a twin-screw extruder equipped with a feeding hopper. After bringing the polymer to the molten state, 6 parts of a mixture of n-pentane/i-pentane with a weight ratio of 70/30, are injected.
The resulting mass is drawn through an extrusion head equipped with holes. The polymer emerging from the holes is cut by a series of rotating knives in contact with the surface of the die in order to obtain substantially spherical beads having an average diameter of about 1.2 mm. The die is immersed in a water bath.
The beads are sent by the stream of water, cooled to 35° C., separated from the water and dried in a stream of warm air.
Ethoxylated amine and the coating are then added to the beads as described in Example 1.
The expansion and moulding were effected as described in Example 1. The thermal conductivity was about 36 and 35.5 mW/mK with 2 and 4% respectively of titanium dioxide.
The thermal conductivity value of 36.7 mW/mK was obtained, on the other hand with a flat sheet containing 2% by weight of BaSO₄, with a density however of 17 g/l.
Table 2 indicates the physical characteristics of expanded blocks obtained from expandable beads modified with titanium dioxide. Also in these cases, the blocks obtained with the beads, object of the present invention, show a drastic increase in the sintering degree with respect to the reference block.

TABLE 1

Contact time (min.) Density (g/l)

Reference 1 20.5

2 17.2

3 15.5

Example 1(1% TiO₂) 1 19.5

2 15.6

3 14.2

THERMAL CONDUCTIVITY

Sheets DENSITY (mW/mK)

Reference 14 g/l 42.5

Sheet 1 (1% TiO₂) 14 g/l 36.7

Sheet 2 (2% TiO₂) 14 g/l 36

Sheet 3 (4% TiO₂) 14.4 g/l 35.5

TABLE 2


Blocks from beads of first and second expansion

Reference
Density (g/l)	16.5	7.8
Cooling time	30′	2′ 30″
Shrinkage (mm)	−7	−5
Sintering (%)	15	20
Sheet 1 (1% TiO₂)
Density (g/l)	15	8.3
Cooling time	25′	2′ 30″
Shrinkage (mm)	−2	−3
Sintering (%)	85	35
Sheet 2 (2% TiO₂)
Density (g/l)	18.1	8
Cooling time	30′	2′
Shrinkage (mm)	−4	−4
Sintering (%)	80	30
Sheet 3 (4% TiO₂)
Density (g/l)	15	8.4
Cooling time	25′	2′ 30″
Shrinkage (mm)	−2	−4
Sintering (%)	80	40

Claims

1-17. (canceled)

18. A process for preparing expandable vinyl aromatic polymers, comprising:

polymerizing one or more vinyl aromatic monomers present as an aqueous suspension in the presence of an inorganic filler having substantially spherical granulometry, an average diameter ranging from 0.01-100 micron, a refractive index higher than 1.6, and a white index equal to or lower than 22, and

adding an expanding agent to the aqueous suspension before, during or after the polymerizing,

wherein white index is defined in “Color Index” (3^rdedition published by The Society of Dyers and Colorists, 1982).

19. The process according to claim 18, wherein the aqueous suspension further comprises one or more polymerizable comonomers in an amount of up to 50% by weight based on the total weight of the monomers.

20. The process according to claim 18, wherein the polymerizing is carried out to form substantially spherical beads of a polymer having an average diameter of from 0.2-2 mm and which comprise the inorganic filler homogeneously dispersed therein.

21. The process according to claim 18, further comprising:

adding one or more flame-retarding agents in an amount of from 0.1-8% by weight based on the weight of the polymer formed in the process, during the polymerizing.

22. The process according to claim 21, wherein the flame-retarding agent is at least one selected from the group consisting of a brominated aliphatic compound, a cycloaliphatic compound and an aromatic compound.

23. The process as claimed in claim 18, wherein the expanding agent is added during the polymerization and the expanding agent is at least one selected from the group consisting of an aliphatic hydrocarbon, a cycloaliphatic hydrocarbon containing from 3 to 6 carbon atoms, a halogenated derivative of a aliphatic hydrocarbon containing from 1 to 3 carbon atoms, carbon dioxide, water and mixtures thereof.

24. The process according to claim 18, wherein the polymerization in suspension takes place through a solution of vinyl aromatic polymer in the monomer, or mixture of monomers, wherein the concentration of polymer ranges from 1-30% by weight.

25. A process for continuously preparing expandable vinyl aromatic polymer in bulk, comprising the following steps in series:

feeding the vinyl aromatic polymer to an extruder together with one or more inorganic fillers, wherein the inorganic filler has a substantially spherical granulometry, an average diameter ranging from 0.01-100 micron, a refractive index higher than 1.6, and a white index as defined in “Color Index” (3^rdedition published by The Society of Dyers and Colorists, 1982) of 22 or lower;

heating the vinyl aromatic polymer to a temperature higher than the relative melting point of the vinyl aromatic polymer;

injecting one or more expanding agents into the molten vinyl aromatic polymer obtained by the heating; and

forming beads by passing the molten vinyl aromatic polymer through a dye,

wherein the beads are substantially spherical and have an average diameter of from 0.2-2 mm and the expanding agent is injected into the molten polymer before the molten polymer is passed through the dye.

26. The process as claimed in claim 25, wherein the expanding agent is injected into the molten polymer as a mixture with one or more additives.

27. The process as claimed in claim 25, wherein the beads formed by passing the molten vinyl aromatic polymer through the dye are expandable.

28. The process as claimed in claim 18, further comprising:

carrying out the polymerizing to form expandable beads and pretreating the beads by

(i) coating the beads with a liquid antistatic agent; and

(ii) applying a coating to the treated beads wherein the coating comprises a mixture of mono-, di- and trimesters of glycerine with one or more fatty acids and one or more metallic stearates.

29. The process as claimed in claim 28, wherein the liquid antistatic agent is at least one selected from the group consisting of an amine, a tertiary ethoxylated alkyl amine, and an ethylene oxide-propylene oxide copolymer.

30. The process as claimed in claim 29, wherein the coating further comprises the inorganic filler.

31. The process as claimed in claim 28, wherein the metallic stearate is at least one selected from the group consisting of zinc stearate and magnesium stearate.

32. A process for continuously preparing expandable vinylaromatic polymers, which comprises the following steps in series:

feeding a vinylaromatic polymer, as described above, to an extruder, together with an inorganic filler, having a substantially spherical granulometry, an average diameter ranging from 0.01 to 100 μm, a refraction index higher than 1.6 and a white index, as defined in “Colour Index” (third edition published by The Society of Dyers and Colourists, 1982), equal to or lower than 22;

heating the vinylaromatic polymer to a temperature higher than the relative melting point;

injecting the expanding agent and possible additives, into the molten polymer, before extrusion through a die; and

forming beads, optionally expandable, through a die, in a substantially spherical form with an average diameter ranging from 0.2 to 2 mm.

33. The process as claimed in claim 32, further comprising:

(i) coating the beads with a liquid antistatic agent; and

(ii) applying a coating to the treated beads wherein the coating comprises a mixture of mono-, di- and tri-esters of glycerine with one or more fatty acids and one or more metallic stearates.

34. The process as claimed in claim 32, wherein the liquid antistatic agent is at least one selected from the group consisting of an amine, a tertiary ethoxylated alkyl amine, and an ethylene oxide-propylene oxide copolymer.

35. The process as claimed in claim 32, wherein the coating further comprises the inorganic filler.

36. The process as claimed in claim 32, wherein the metallic stearate is at least one selected from the group consisting of zinc stearate and magnesium stearate.