Expandable vinyl aromatic polymers
AssigneeTotalenergies Onetech Belgium
InventorsJacques Michel, Jean-Claude Deleye, Amelio Iacolina, Magali Vachaudez, Laetitia Urbanczyk, Michel Cassart
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Abstract
The present invention is related to expandable vinyl aromatic polymers comprising comminuted coke, said comminuted coke having an average stack height (Lc) of carbon crystallites at least 4 nm, a volume median particle diameter (D50) comprised between 1 and less than 5 μm and being characterized by a span (D90−D10)/D50 below 2.5 Molded parts produced from the expandable vinyl aromatic polymers prove low thermal conductivities for a low foam density.
Claims12
Expandable vinyl aromatic polymers comprising at least one blowing agent and a plurality of dispersed coke particles, said dispersed coke particles being characterized by:
- (i) an average stack height (Lc) of carbon crystallites of at least 4 nm, wherein Lc is given by the formula
- L
- c
-
- (
- nm
- )
- =
- 0.89
- *
- 0.154
- β
- *
- cos
-
- (
- θ
- )
- and is estimated from the full width at half maximum of diffraction peak [002];
- (ii) a volume median particle diameter (D50) comprised between 1 and 5 μm, as obtained from laser light scattering measurements according to ISO 13320;
- and
- (iii) a span (D90−D10)/D50 below 2.5 as obtained from laser light scattering measurements according to ISO 13320;
- wherein the expandable vinyl aromatic polymers comprise between 4 and 6% by weight of the dispersed coke particles;
- and
- wherein polymer foams obtained from the molding of expanded polymer pellets of the expandable vinyl aromatic polymers comprise a thermal conductivity, (λ), measured according to ISO 8301, of 31.0 mW/mK or less at a foam density of 12.5 kg/m3 or higher.
A process for the preparation of pellets of expandable vinyl aromatic polymers, said process comprising the steps of:
- a. producing a polymer melt stream of expandable vinyl aromatic polymers
- b. deriving a part of said polymer melt stream and creating a main polymer melt stream (1) and a side loop with an additional polymer melt stream (2);
- c. dispersing a plurality of coke particles and a foam cell regulator into said additional polymer melt stream (2), said plurality of coke particles being characterized by:
- (i) an average stack height (Lc) of carbon crystallites of at least 4 nm, wherein Lc is given by the formula
- L
- c
- (
- nm
- )
- =
- 0.89
- *
- 0.154
- β
- *
- cos
-
- (
- θ
- )
- and is estimated from the full width at half maximum of diffraction peak [002];
- (ii) a volume median particle diameter (D50) comprised between 1 and 7 μm, as obtained from laser light scattering measurements according to ISO 13320;
- and
- (iii) a span (D90−D10)/D50 below 3.0 as obtained from laser light scattering measurements according to ISO 13320;
- d. joining the additional polymer melt stream (2) and the main polymer melt stream (1) to form a new polymer melt stream;
- e. introducing a blowing agent into the new polymer melt stream;
- f. cooling the new polymer melt stream comprising all ingredients down to a temperature of 200° C. or less;
- g. discharging the new polymer melt stream through a die plate with holes;
- and
- h. pelletizing the new polymer melt stream under water with a pressure above 3 bar;
- wherein the dispersing is such that the pellets of expandable vinyl aromatic polymers comprise between 4 and 6% by weight of coke;
- wherein the dispersed coke particles are characterized by:
- (i) an average stack height (Lc) of carbon crystallites of at least 4 nm,
- (ii) a volume median particle diameter (D50) comprised between 1 and 5 μm as obtained from laser light scattering measurements according to ISO 13320;
- and
- (iii) a span (D90−D10)/D50 below 2.5 as obtained from laser light scattering measurements according to ISO 13320;
- and
- wherein polymer foams obtained from the molding of expanded vinyl aromatic polymer pellets of the expandable vinyl aromatic polymers comprise a thermal conductivity (λ), measured according to ISO 8301, of 31.0 mW/mK or less at a foam density of 12.5 kg/m3 or higher.
Polymer foams obtained from the molding of expanded polymer pellets of expandable vinyl aromatic polymers comprising at least one blowing agent and a plurality of dispersed coke particles, said dispersed coke particles being characterized by:
- an average stack height (Lc) of carbon crystallites of at least 4 nm;
- wherein Lc is given by the formula
- L
- c
-
- (
- nm
- )
- =
- 0.89
- *
- 0.154
- β
- *
- cos
-
- (
- θ
- )
- and is estimated from the full width at half maximum of diffraction peak [002];
- a volume median particle diameter (D50) comprised between 1 and 5 μm, as obtained from laser light scattering measurements according to ISO 13320;
- and
- a span (D90−D10)/D50 below 2.5 as obtained from laser light scattering measurements according to ISO 13320;
- where the expandable vinyl aromatic polymers comprise between 4 and 6% by weight of the dispersed coke particles;
- and
- wherein said polymer foams are characterized by a thermal conductivity (λ), measured according to ISO 8301, of 31.0 mW/mK or less at a foam density of 12.5 kg/m3 or higher.
Dependencies are inferred from the claim text.