Polyurethane filled tires

1. A tire comprising a cellular polyurethane or polyurethane-urea elastomeric material made from the reaction of:

i) a polyisocyanate composition having a free NCO-value of 15-25% by weight comprising an isocyanate-terminated prepolymer which is the reaction product of an excess of an organic polyisocyanate and a polyether polyol having an average nominal hydroxyl functionality of 2-6, a number average molecular weight of 2000-6000 and an oxyethylene content of 20-35% by weight, wherein at least 50% of the oxyethylene groups are present at the end of the polyether polyol;

ii) a polymer polyetherpolyol wherein the polymer polyetherpolyol consists of (a) at least one polyetherpolyol having a maximum oxyethylene content of 20% by weight calculated on the total weight of the at least one polyetherpolyol, (b) a second polyetherpolyol having an oxyethylene content of 10-20% by weight calculated on the total weight of the second polyetherpolyol, and (c) solid particles; and wherein a mixture of (a) and (b) has a weighted average molecular weight in the range of 4000-7000 and wherein the amount of solid particles is in the range of 15-35 wt % calculated on the total weight of the polymer polyetherpolyol;

iii) a chain extender;

iv) at least one of a catalyst and crosslinker; and

v) a blowing agent, said cellular polyurethane or polyurethane-urea elastomeric material having the following properties:

Shore A hardness according to ASTM D2240 of at least 45 and lower than 85;

Compression set at room temperature lower than 10% and at 70° C. lower than 40% according to ASTM D395; and

Ball rebound according to ASTM D3574 of at least 40% and wherein the tire is filled with the elastomeric material.

2. A tire according to claim 1 , wherein the tire is a low speed vehicle tire.

3. A tire according to claim 1 , wherein the elastomeric material has a moulded density in the range 400-700 kg/m 3 according to ISO 845.

4. A reaction system comprising:

i) a polyisocyanate composition having a free NCO-value of 15-25% by weight comprising an isocyanate-terminated prepolymer which is the reaction product of an excess of an organic polyisocyanate and a polyether polyol having an average nominal hydroxyl functionality of 2-6, a number average molecular weight of 2000-6000 and an oxyethylene content of 20-35% by weight, wherein at least 50% of the oxyethylene groups are present at the end of the polyether polyol;

ii) a polymer polyetherpolyol wherein the polymer polyetherpolyol consists of (a) at least one polyetherpolyol having a maximum oxyethylene content of 20% by weight calculated on the total weight of the at least one polyetherpolyol, (b) a second polyetherpolyol having an oxyethylene content of 10-20% by weight calculated on the total weight of the second polyetherpolyol, and (c) solid particles, and wherein a mixture of (a) and (b) has a weighted average molecular weight in the range of 4000-7000 and wherein the amount of solid particles is in the range of 15-35 wt % calculated on the total weight of the polymer polyetherpolyol;

iii) at least one of a chain extender and cross-linker;

iv) a catalyst; and

v) a blowing agent,

and wherein the reaction system, upon reacting, provides a cellular polyurethane elastomeric material having the following properties: a shore A hardness according to ASTM D2240 of at least 45 and lower than 85; a compression set at room temperature lower than 10% and at 70° C. lower than 40% according to ASTM D395; and a ball rebound according to ASTM D3574 of at least 40%.

5. A reaction system according to claim 4 , wherein the organic polyisocyanate used in the preparation of the polyisocyanate composition is selected from an aliphatic polyisocyanate, a cycloaliphatic polyisocyanate, an araliphatic polyisocyanate and a mixture thereof.

6. A reaction system according to claim 4 , wherein the polyether polyol used for preparing the prepolymer has an average nominal functionality of 2-4 and a number average molecular weight of 3000-5000.

7. A reaction system according to claim 4 , wherein the polyether polyol used for preparing the prepolymer is obtained from the polymerization of ethylene oxide with propylene oxide in the presence of a diol and/or a triol.

8. A reaction system according to claim 4 , wherein (a) the at least one polyetherpolyol has an oxyethylene content of 10-20% by weight and wherein the oxyethylene groups are present at the end of the at least one polyetherpolyol.

9. A reaction system according to claim 4 , wherein the solid particles comprise styrene based polymer particles.

10. A reaction system according to claim 4 , wherein

(a) the at least one polyetherpolyol has a molecular weight in the range of 5000-7000 and an oxyethylene content of 10-20% by weight and the oxyethylene groups are present at the end of (a) the at least one polyetherpolyol, and

(b) the second polyetherpolyol has oxyethylene groups present at the end of (b) the second polyetherpolyol.

11. A reaction system according to claim 10 , wherein

the ratio of

(a) the at least one polyetherpolyol to (b) the second polyetherpolyol is in the range of 80/20 to 40/60.

12. A reaction system according to claim 4 , wherein the blowing agent is selected from a hydrofluorocarbon compound, an acetal based compound, water and a mixture thereof.

13. A reaction system according to claim 4 , wherein the blowing agent is an acetal based compound and is present in the range of 4-8 wt % calculated on the total weight of the reaction system.

14. A reaction system according to claim 4 , wherein the blowing agent is water and is present in the range of at least 0.3 parts by weight per 100 parts by weight of the reaction system.

15. A reaction system according to claim 4 , wherein the chain extender is a polyol having a hydroxyl functionality of 2-6 and a molecular weight of 62-499 and wherein the amount of chain extender present is at most 15 parts by weight per 100 parts by weight of polymer polyetherpolyol.

16. A reaction system according to claim 15 , wherein the chain extender is monoethylene glycol, butanediol, or hexanediol.

17. A process for making a cellular polyurethane elastomer said process comprising reacting at an isocyanate index in the range 90-110 the reaction system according to claim 4 in a mould.

18. A process according to claim 17 wherein the polymer polyetherpolyol is premixed with the at least one of a chain extender and crosslinker, the catalyst and the blowing agent and then reacted with the polyisocyanate composition.

19. A process for making a tire made of a cellular polyurethane or polyurethane-urea elastomeric material comprising:

i) providing a polymer polyetherpolyol wherein the polymer polyetherpolyol consists of: (a) at least one polyetherpolyol having a molecular weight in the range of 5000-7000 and a maximum oxyethylene content of maximum 20% by weight calculated on the total weight of the at least one polyetherpolyol, (b) a second polyetherpolyol having a molecular weight of 4000-6000 and an oxyethylene content of 10-20% by weight calculated on total weight of the second polyetherpolyol, and (c) solid particles, wherein the amount of solid particles is in the range of 15-35 wt % calculated on the total weight of the polymer polyetherpolyol; a catalyst; a blowing agent; and at least one of a chain extender and crosslinker; and then

ii) mixing a polyisocyanate composition with the polymer polyol composition of step i) to form a mixed polyisocyanate composition, wherein the polyisocyanate composition has a free NCO-value of 15-25% by weight comprising an isocyanate-terminated prepolymer which is the reaction product of an excess of an organic polyisocyanate and a polyether polyol having an average nominal hydroxyl functionality of 2-6, a number average molecular weight of 2000-6000 and an oxyethylene content of 20-35% by weight, wherein at least 50% of the oxyethylene groups are present at the end of the polyether polyol; and then

iii) casting the mixed polyisocyanate composition obtained in step ii) into a mould to obtain a reacted polyisocyanate composition, and then

iv) curing the reacted polyisocyanate composition obtained in step iii) at an elevated temperature, and then

v) demoulding the obtained tire made of polyurethane cellular elastomer wherein the elastomeric material has the following properties: a shore A hardness according to ASTM D2240 of at least 45 and lower than 85; a compression set at room temperature lower than 10% and at 70° C. lower than 40% according to ASTM D395; and a ball rebound according to ASTM D3574) of at least 40%.

20. A process according to claim 19 , wherein the step of mixing of the polyisocyanate composition with the polymer polyol composition obtained in step i) is performed using a 2 component high pressure mixing system or a 2 component dynamic mixing system and wherein the step of casting the mixed polyisocyanate composition obtained in step ii) is performed using an open mould, and wherein the step of curing the reacted polyisocyanate composition obtained in step iii) is performed at an elevated temperature in the range 50°−60° C.