Copolycarbonate and composition containing the same
US-2016376405-A1 · Dec 29, 2016 · US
US10167364B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10167364-B2 |
| Application number | US-201615552219-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 15, 2016 |
| Priority date | Feb 18, 2015 |
| Publication date | Jan 1, 2019 |
| Grant date | Jan 1, 2019 |
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The present invention relates to a process for preparing aromatic polycarbonates, comprising the step of reacting bisphenols with dithiocarbonates or selenium analogs thereof in the presence of a catalyst. It further relates to the use of dithiocarbonates or selenium analogs thereof as transesterifying reagents for the preparation of polycarbonates.
Opening claim text (preview).
The invention claimed is: 1. A process for preparing polycarbonates, comprising reacting bisphenols with a transesterifying reagent in the presence of a catalyst, wherein the transesterifying reagent comprises a compound of the general formula (I): R—X—C(O)—X′—R′ (I) wherein X and X′ are each independently S or Se, and R and R′ are each independently alkyl or aryl or R and R′ together are an alkylene chain. 2. The process according to claim 1 , wherein X and X′ in the general formula (I) are S. 3. The process according to claim 1 , wherein the compounds R—X—H and R′—X′—H formed during the reaction are removed continuously. 4. The process according to claim 1 , wherein the reaction is conducted for a first period of time at a first temperature and a first pressure and then for a second period of time at a second temperature and a second pressure, and wherein the second temperature is greater than the first temperature and the second pressure is lower than the first pressure. 5. The process according to claim 4 , wherein the first temperature is 150° C. to 210° C. and the second temperature is 210° C. to 400° C. 6. The process according to claim 4 , wherein the first pressure is 200 mbar to 900 mbar and the second pressure is 1 mbar to 200 mbar. 7. The process according to claim 4 , wherein the reaction conducted for the second period of time at the second temperature and the second pressure is conducted in an evaporating extruder, a disc reactor or an evaporating calender. 8. The process according to claim 1 , wherein R and R′ in the general formula (I) are methyl, ethyl or phenyl. 9. The process according to claim 1 , wherein the transesterifying reagent is a dialkyl dithiocarbonate. 10. The process according to claim 1 , wherein the polyols used include bisphenol A, bisphenol F, or bisphenol TMC. 11. The process according to claim 1 , wherein the catalyst is a phosphonium salt or a bicyclic amine. 12. The process according to claim 1 , wherein the catalyst is added in two or more portions over the course of the reaction. 13. The process according to claim 1 , further comprising adding a diaryl carbonate or dialkyl carbonate to the reaction product obtained. 14. A transesterifying reagent for the preparation of polycarbonates comprising a compound of the general formula (I): R—X—C(O)—X′—R′ (I), wherein X and X′ are S or Se, and R and R′ are each independently alkyl or aryl or R and R′ together are an alkylene chain. 15. The process according to claim 5 , wherein the first pressure is 200 mbar to 900 mbar and the second pressure is 1 mbar to 200 mbar.
characterised by the apparatus used · CPC title
using other monomers · CPC title
controlling the pressure · CPC title
Selenium; Compounds thereof · CPC title
Controlling the temperature · CPC title
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