Process for reducing the VOC content of plastomers

1. A process for reducing the volatile organic compound (VOC) content of plastomers the process comprising the steps of

a) subjecting the plastomer in granular form containing VOCs which is contained in an aeration vessel to a gas flow,

and

b) withdrawing granular plastomer from the aeration vessel which has a lower content of VOCs,

wherein the average particle size of the granular plastomer is greater than 2.5 mm,

wherein the gas has a minimum temperature of at least 26° C. measured at a gas inlet of the aeration vessel, and a maximum temperature of 4° C. below the Vicat temperature (10N, ISO 306) of the granular plastomer or 35° C. measured at the gas inlet of the aeration vessel, whichever value is lower, and

wherein at least a part of the withdrawn granular plastomer is recirculated to the aeration vessel.

2. The process according to claim 1 ,

wherein the recirculation rate of the granular plastomer recirculated to the aeration vessel is between 0.25 and 10 percent per hour.

3. The process according to claim 1 ,

wherein the gas flow in step a) is within the range of 5 m 3 /(h·t) to 150 m 3 /(h·t).

4. The process according to claim 1 ,

wherein the gas stream in step a) is within the range of 5.0 l/(h·cm 2 ) to 50.0 l/(h·cm 2 ).

5. The process according to claim 1 ,

wherein the aeration time in step a) is less than 40 hours.

6. The process according to claim 1 ,

wherein step a) is run for at least 2 hours.

7. The process according to claim 1 ,

wherein the plastomers are homo- or copolymers of ethylene.

8. The process according to claim 1 ,

wherein the granular plastomer in step a) has a density of equal or lower than 900 kg/m 3 .

9. The process according to claim 1 ,

wherein the granular plastomer in step a) has a MFR2 of 25.0 g/10 min or lower (ISO 1133 at 2.16 kg load and 190° C.).

10. The process according to claim 1 ,

wherein the granular plastomer withdrawn in step b) has a VOC content (VOC, VDA277) of below 65 ppm.

11. The process according to claim 1 ,

wherein the process is used in a continuous polymerization process.

12. The process according to claim 1 ,

wherein the recirculation of the at least a part of the withdrawn granular plastomer to the aeration vessel is conducted at a velocity of less than 15 m/s.

13. The process according to claim 1 ,

wherein the aeration vessel comprises a silo comprising a main vertical cylinder and a conical section at the bottom of the cylinder, and

wherein the cone angle of the conical section is less or equal 40°.

14. The process according to claim 1 ,

wherein the gas used in step a) is N 2 containing gas.

15. The process according to claim 1 ,

wherein the gas in step a) is injected from the bottom of the aeration vessel.

16. The process of claim 1 , wherein the average particle size of the granular plastomer is greater than 2.7 mm.

17. The process of claim 1 , wherein the average particle size of the granular plastomer is greater than 3.0 mm.

18. The process of claim 1 , wherein the plastomers are copolymers of ethylene and octene.

19. The process of claim 1 , wherein the granular plastomer in step a) has a density of equal or lower than 883 kg/m 3 .

20. The process of claim 1 , wherein the gas used in step a) is air.