Granular thermal insulation material and method for producing the same
The present invention relates to a granular thermal insulation material comprising hydrophobized silicon dioxide and at least one IR opacifier, having a tamped density of up to 250 g/l and a compressive strength according to DIN EN 826:2013 at 50% compression of 150 to 300 kPa or greater than 300 kPa, to processes for production thereof and to the use thereof for thermal insulation.
1. A granular material comprising hydrophobized silicon dioxide and at least one IR opacifier, wherein said granular material comprises:
a) a tamped density of up to 250 g/l; and
b) a compressive strength according to DIN EN 826:2013 at 50% compression of greater than 300 kPa, wherein the compressive strength is measured on a bed with a square face having an edge length of 200 mm and bed height 20 mm.
2. The granular material of claim 1 , wherein the IR opacifier is selected from the group consisting of: silicon carbide; titanium dioxide; zirconium dioxide; ilmenites; iron titanates; iron oxides; zirconium silicates; manganese oxides; graphites; carbon blacks; and mixtures thereof.
3. The granular material of claim 1 , wherein said granular material comprises a BET surface area of 50 to 400 m 2 /g.
4. The granular material of claim 1 , wherein said granular material comprises a tamped density of 100 to 240 g/l.
5. The granular material of claim 1 , wherein said granular material comprises a compressive strength according to DIN EN 826:2013 at 50% compression of greater than 300 kPa to 2000 kPa, wherein the compressive strength is measured on a bed with a square face having an edge length of 200 mm and bed height 20 mm.
6. The granular material of claim 1 , wherein said granular material comprises a thermal conductivity of less than 50 mW/(m*K) according to EN 12667:2001, measured in the bed, at a mean measurement temperature of 10° C., a contact pressure of 250 Pa under an air atmosphere and at standard pressure.
7. The granular material of claim 1 , wherein the silicon dioxide has been produced by pyrogenic means.
8. The granular material of claim 1 , wherein said granular material comprises a methanol wettability of methanol content 10% to 60% by weight in a methanol/water mixture.
9. The granular material of claim 2 , wherein said granular material comprises a BET surface area of 50 to 400 m 2 /g.
10. The granular material of claim 2 , wherein said granular material comprises a tamped density of 100 to 240 g/l.
11. The granular material of claim 2 , wherein said granular material comprises a compressive strength according to DIN EN 826:2013 at 50% compression of greater than 300 kPa to 2000 kPa, wherein the compressive strength is measured on a bed with a square face having an edge length of 200 mm and bed height 20 mm.
12. The granular material of claim 2 , wherein said granular material comprises a thermal conductivity of less than 50 mW/(m*K) according to EN 12667:2001, measured in the bed, at a mean measurement temperature of 10° C., a contact pressure of 250 Pa under an air atmosphere and at standard pressure.
13. The granular material of claim 12 , wherein said granular material comprises a compressive strength according to DIN EN 826:2013 at 50% compression of greater than 300 kPa to 2000 kPa, wherein the compressive strength is measured on a bed with a square face having an edge length of 200 mm and bed height 20 mm.
14. The granular material of claim 13 , wherein said granular material comprises a tamped density of 100 to 240 g/l.
15. The granular material of claim 2 , wherein said granular material comprises a methanol wettability of methanol content 10% to 60% by weight in a methanol/water mixture.
16. A process for producing the granular material of claim 1 , comprising the following steps:
a) mixing a hydrophilic silicon dioxide with at least one IR opacifier;
b) densifying the mixture obtained in step a) to give a granular material;
c) either:
i) subjecting the granular material produced in step b) to thermal treatment at a temperature of 200 to 1200° C.; or
ii) treating the granular material produced in step b) with ammonia;
d) hydrophobizing the granular material produced in step c) with a hydrophobizing agent.
17. The process of claim 16 , wherein step c)i) is conducted at 800-1100° C.
18. The process of claim 16 wherein, step b) and/or c) and/or d) is followed by a separation of fractions of the granular material of different size from one another.
19. The process of claim 16 , wherein the hydrophobizing agent used in step d) is selected from the group consisting of halosilanes, alkoxysilanes, silazanes and siloxanes.
20. The process of claim 16 , wherein the granular material comprises a thermal conductivity of less than 50 mW/(m*K) according to EN 12667:2001, measured in the bed, at a mean measurement temperature of 10° C., a contact pressure of 250 Pa under an air atmosphere and at standard pressure.