Apparatus
Process for producing a polymer product in a slurry polymerization process, which slurry polymerization process includes a slurry heater for heating a stream of polymer product slurry withdrawn from a slurry reactor. The process includes reconfiguring the slurry heater from an initial slurry heater configuration to a subsequent slurry heater configuration and further where the slurry heater is reconfigured to form a subsequent slurry heater having a different total length and/or a different average internal diameter than the initial slurry heater.
1. A process for the production of polymer product in a slurry polymerisation process, which slurry polymerisation process comprises a slurry heater for heating a stream of polymer product slurry withdrawn from a slurry reactor, wherein said process comprises reconfiguring the slurry heater from an initial slurry heater configuration to a subsequent slurry heater configuration and further wherein the slurry heater is reconfigured to form a subsequent slurry heater having a different total length and/or a different average internal diameter than the initial slurry heater.
2. A process according to claim 1 wherein the slurry heater apparatus comprises at least 3 different heating sections, at least two of said heating sections being connected in fluid communication in series to form the initial slurry heater, wherein the slurry heater apparatus is adapted such that it can be reconfigured to form said subsequent slurry heater, said subsequent slurry heater also comprising at least two of said heating sections connected in fluid communication in series.
3. A method for transitioning from the production of a first polymer product to the production of a second polymer product in a slurry polymerisation process, which slurry polymerisation process comprises a slurry heater for heating a stream of polymer product slurry withdrawn from a slurry reactor, wherein said method comprising reconfiguring the slurry heater from an initial slurry heater configuration to a subsequent slurry heater configuration and further wherein the slurry heater is reconfigured to form a subsequent slurry heater having a different total length and/or a different average internal diameter than the initial slurry heater.
4. A method according to claim 3 wherein the slurry heater apparatus comprises at least 3 different heating sections, at least two of said heating sections being connected in fluid communication in series to form the initial slurry heater, wherein the slurry heater apparatus is adapted such that it can be reconfigured to form said subsequent slurry heater, said subsequent slurry heater also comprising at least two of said heating sections connected in fluid communication in series.
5. A process according to claim 2 wherein each heating section is between 2 and 20 meters in length.
6. A process according to claim 2 wherein the overall length of the initial and subsequent slurry heaters are at least 50 m and up to 500 m.
7. A process according to claim 2 wherein each heating section has an internal diameter, d, of at least 20 mm and up to 200 mm.
8. A process according to claim 2 wherein the slurry heater apparatus comprises in total 5 to 150 heating sections.
9. A process according to claim 8 wherein the slurry heater apparatus comprises in total 30 to 100 heating sections.
10. A process according to claim 2 wherein there are provided at least two initial slurry heaters each comprising at least two heating sections connected in series.
11. A process according to claim 2 wherein there are provided at least two subsequent slurry heaters each comprising at least two heating sections connected in series.
12. A process according to claim 10 wherein there are provided at least two subsequent slurry heaters each comprising at least two heating sections connected in series.
13. A method according to claim 4 wherein each heating section is between 2 and 20 meters in length.
14. A method according to claim 4 wherein the overall length of the initial and subsequent slurry heaters are at least 50 m and up to 500 m.
15. A method according to claim 4 wherein each heating section has an internal diameter, d, of at least 20 mm and up to 200 mm.
16. A method according to claim 4 wherein the slurry heater apparatus comprises in total 5 to 150 heating sections.
17. A method according to claim 16 wherein the slurry heater apparatus comprises in total 30 to 100 heating sections.
18. A method according to claim 4 wherein there are provided at least two initial slurry heaters each comprising at least two heating sections connected in series.
19. A method according to claim 4 wherein there are provided at least two subsequent slurry heaters each comprising at least two heating sections connected in series.
20. A method according to claim 18 wherein there are provided at least two subsequent slurry heaters each comprising at least two heating sections connected in series.