Process for the production of water and solvent-free polymers

1. A process for removing volatile compounds from a fluid comprising at least one synthetic rubber and at least one volatile compound, the process comprising:

a) heating the fluid to a first temperature to form a heated fluid, and removing a portion of the volatile compounds from the heated fluid via vacuum in a degassing vessel at a first pressure to obtain a free-flowing concentrated fluid, wherein the first pressure and first temperature are configured to obtain a concentrated fluid comprising 10-60 wt % non-volatile polymer and 40-90 wt % volatile compounds;

b) reheating the concentrated fluid to a second temperature to obtain a reheated free-flowing concentrated fluid; and

c) extruding the reheated concentrated fluid in an extruder comprising at least one degassing section, and removing at least an additional portion of the volatile compounds from the reheated concentrated fluid via vacuum in the at least one degassing section at a second pressure to obtain a non-volatile polymer product having a content of volatile compounds of less than 0.5 wt % water and less than 0.75 wt % volatile organic compounds based on the total mass of the non-volatile polymer.

2. The process according to claim 1 , wherein the viscosity of the reheated concentrated fluid is 500 mPa to 50,000,000 mPa.

3. The process according to claim 1 , wherein the content of volatile compounds in the non-volatile polymer is less than 1 wt % based on the total mass of the non-volatile polymer.

4. The process according to claim 1 , wherein the at least one synthetic rubber comprises at least one halogenated butyl rubber.

5. The process according to claim 1 , wherein the fluid contains from 3 wt % to 50 wt % polymer and from 60 wt % to 97 wt % volatile compounds, wherein the total amount of polymer and volatile compounds comprise 90 to 100 wt % of the total mass of the fluid.

6. The process according to claim 1 , wherein the fluid has a viscosity of 100 mPa to 25,000 mPa.

7. The process according to claim 1 , wherein:

the first temperature is 100° C. to 200° C.;

the first pressure is 100 hPa to 4,000 hPa;

the second temperature is 50° C. to 200° C.; and

the second pressure is 1 hPa to 2,000 hPa.

8. The process according to claim 1 , wherein:

the process, prior to a), further comprises:

a1) treating a crude fluid comprising one or more of a non-volatile polymer, at least one volatile organic compound, at least one hydrophilic compound, and combinations thereof, by mixing the crude fluid with water to obtain an organic phase comprising primarily non-volatile polymer and volatile organic compounds, and an aqueous phase comprising water and hydrophilic compounds, and

a2) separating the aqueous phase from the organic phase, wherein the organic phase is the fluid and comprises 3-50 wt % non-volatile polymer and 60-97 wt % volatile compounds which together add up to 95 100 wt % of the fluid;

the process further comprises serially repeating step a) at least one additional time;

the first temperature is 120° C. to 175° C.;

the first pressure is 230 hPa to 1,100 hPa;

the first pressure and first temperature are configured to obtain a concentrated fluid comprising 25-60 wt % non-volatile polymer and 40-75 wt % volatile compounds;

the second temperature is 90° C. to 180° C.; and

the second pressure is 5 hPa to 900 hPa and the non-volatile polymer has a content of volatile compounds of less than 0.075 wt % water and less than 0.1 wt % volatile organic compounds based on the total mass of the non-volatile polymer.

9. The process according to claim 1 , wherein extruding further comprises controlling the temperature in different zones of the extruder during extruding independently of each other at different temperatures and, wherein the separate zones are independently heated, unheated, or cooled.

10. The process according to claim 1 , wherein the extruding further comprises accumulating pressure to facilitate the evaporation of volatile compounds.

11. The process according to claim 10 , wherein accumulating pressure is repeated during extruding.

12. The process according to claim 1 , further comprising processing the non-volatile polymer product.

13. The process according to claim 1 , further comprising cooling the non-volatile polymer product.

14. The process according to claim 1 , wherein extruding is performed at a feed rate of 5 kilograms per hour to 25,000 kilograms per hour.

15. The process according to claim 1 , wherein extruding further comprises applying a stripping agent.

16. The process according to claim 1 , further comprising adding one or more additives to the fluid prior to heating, adding one or more additives to the reheated concentrated fluid during extruding, or combinations thereof.

17. The process according to claim 1 , further comprising repeating step a).

18. The process according to claim 17 , wherein the repeating of step a) is performed multiple times in series.

19. The process according to claim 1 , further comprising regulating the pressure during the heating, the reheating, the extruding, or combinations thereof.

20. The process according to claim 1 , wherein the fluid is obtained by a process of removing hydrophilic compounds from a crude fluid comprising one or more of a polymer, a volatile organic compound, a hydrophilic compound, and combinations thereof, wherein the process comprises:

a1) treating the crude fluid by mixing the crude fluid with water to obtain an organic phase comprising primarily non-volatile polymer and volatile organic compounds and an aqueous phase comprising water and hydrophilic compounds, and

a2) separating the organic phase from the aqueous phase, wherein the organic phase is the fluid for step a).

21. The process according to claim 20 , wherein the separating further comprising coalescing the organic phase and the aqueous phase.

22. The process according to claim 20 , further comprising repeating step a1).

23. The process according to claim 22 , wherein the repeating of step a1) is performed multiple times in series.

24. The process according to claim 20 , wherein the separating is performed at temperatures of greater than 40° C.