Process for producing pellets of copolymers of propylene
US-2017341267-A1 · Nov 30, 2017 · US
US10393455B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10393455-B2 |
| Application number | US-201414903332-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 15, 2014 |
| Priority date | Jul 22, 2013 |
| Publication date | Aug 27, 2019 |
| Grant date | Aug 27, 2019 |
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Method for treating a heat exchanger which in operation is used to cool process water which has been in contact with polymer particles. The method includes passing to the process side of the heat exchanger a treatment stream while the heat exchanger is at an elevated temperature compared to the temperature when the heat exchanger is in operation.
Opening claim text (preview).
The invention claimed is: 1. A method for treatment of a heat exchanger which in operation is used to cool process water which has been in contact with polymer particles, which method comprises passing to the process side of the heat exchanger a treatment stream whilst the heat exchanger is at an elevated temperature compared to the temperature when the heat exchanger is in operation, the treatment stream also being an aqueous stream, and wherein the polymer particles are selected from polyethylene and polypropylene particles and further wherein the polymer particles with which the process water has been in contact comprise additives which have been added prior to or during pelletising, which are insoluble in the process water and have a melting point of 45° C. to 110° C. 2. A method according to claim 1 wherein the process water is used to convey polymer particles from one location to another and is then separated from the polymer particles and passed to the heat exchanger to be cooled prior to being used again. 3. A method according to claim 1 wherein the process water is process water for underwater pelletising operations. 4. A method according to claim 1 wherein the polymer particles with which the process water has been in contact comprise erucamide and silica. 5. A method according to claim 1 wherein during the treatment the heat exchanger is at a temperature at least 5° C. higher than the temperature when the heat exchanger is in operation. 6. A method according to claim 1 wherein cooling medium is not passed through the heat exchanger during the treatment. 7. A method according to claim 1 wherein the aqueous stream comprises fresh water. 8. A method according to claim 7 wherein the fresh water is water which is added as “make-up water” to the process water. 9. A method according to claim 1 wherein the treatment stream comprises a portion of the process water which is used in operation. 10. A method according to claim 4 wherein during the treatment the heat exchanger is at a temperature at least 5° C. higher than the temperature when the heat exchanger is in operation. 11. A method according to claim 4 wherein cooling medium is not passed through the heat exchanger during the treatment. 12. A method according to claim 4 wherein the treatment stream is also an aqueous stream. 13. A method according to claim 12 wherein the aqueous stream comprises fresh water. 14. A method according to claim 13 wherein the fresh water is water which is added as “make-up water” to the process water. 15. A method according to claim 4 wherein the treatment stream comprises a portion of the process water which is used in operation. 16. A method according to claim 1 wherein during treatment, the temperature of the heat exchanger is from 50° C. to 80° C. 17. A method according to claim 4 wherein during treatment, the temperature of the heat exchanger is from 50° C. to 80° C.
cleaning by increasing the temperature of heat exchange surfaces (F28G7/005, F28G11/00 take precedence) · CPC title
Radiators for recooling a coolant of cooling systems · CPC title
Auxiliary treatment of granules · CPC title
under-water, e.g. underwater pelletizers · CPC title
by heating (B08B7/0035 takes precedence) · CPC title
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