Low shear process for polycarbonate purification
US-2016168322-A1 · Jun 16, 2016 · US
US9617380B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9617380-B2 |
| Application number | US-201414907369-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 25, 2014 |
| Priority date | Jul 25, 2013 |
| Publication date | Apr 11, 2017 |
| Grant date | Apr 11, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
In an embodiment, a process of purifying a polycarbonate comprises: polymerizing a dihydroxy compound and a carbonate source via an interfacial reaction in the presence of a catalyst to form a product mixture comprising an aqueous phase and an organic phase, wherein the organic phase comprises the polycarbonate, the catalyst, ions, and a solvent having a boiling point T b ; heating the product mixture to greater than or equal to T b ; separating the aqueous phase and the organic phase at a temperature greater than or equal to T b to form a separated organic phase and a separated aqueous phase; extracting the catalyst from the separated organic phase; and extracting the ions from the separated organic phase; wherein if a centrifuge is used in the extracting of the catalyst, the extracting of the ions, or both, the process further comprises cooling a stream entering the centrifuge to less than T b .
Opening claim text (preview).
We claim: 1. A process of purifying a polycarbonate comprising: polymerizing a dihydroxy compound and a carbonate source via an interfacial reaction in the presence of a catalyst to form a product mixture comprising an aqueous phase and an organic phase, wherein the organic phase comprises the polycarbonate, the catalyst, ions, and a solvent having a boiling point T b at atmospheric pressure; heating the product mixture to a temperature greater than or equal to the boiling point T b to form a heated product mixture; separating the aqueous phase and the organic phase of the heated product mixture at a temperature greater than or equal to the boiling point T b to form a separated organic phase and a separated aqueous phase; extracting the catalyst from the separated organic phase; and extracting the ions from the separated organic phase to form a purified polycarbonate; wherein if a centrifuge is used in the extracting of the catalyst, the extracting of the ions, or both, the process further comprises cooling a stream entering the centrifuge to a temperature less than the boiling point T b . 2. A process of purifying polycarbonate comprising: polymerizing a dihydroxy compound and a carbonate source via an interfacial reaction in the presence of a catalyst to provide a product mixture comprising an aqueous phase and an organic phase, wherein the organic phase comprises the polycarbonate, the catalyst, ions, and a solvent having a boiling point T b at atmospheric pressure; separating the aqueous phase and the organic phase via a centrifuge to form a separated organic phase and a separated aqueous phase; heating the separated organic phase to a temperature greater than or equal to the boiling point T b to form a heated separated organic phase; extracting the catalyst from the heated separated organic phase; and extracting the ions from the heated separated organic phase to form a purified polycarbonate; wherein at least one of the extracting the catalyst and the extracting the ions occurs by other than a centrifuge at a temperature greater than or equal to the boiling point T b , and if the extracting the catalyst or the extracting the ions occurs with a centrifuge, then the heating occurs after the extracting the catalyst or the extracting the ions occurs with the centrifuge, or the process further comprises cooling a stream entering the centrifuge to a temperature of less than the boiling point T b . 3. The process of claim 1 , wherein the separating occurs via a separating coalescer, a decanter, or a combination comprising one or more of the foregoing. 4. The process of claim 3 , wherein the separating occurs via a decanter. 5. The process of claim 1 , wherein the extracting of the catalyst occurs before the extracting of the ions. 6. The process of claim 1 , wherein the extracting of the catalyst and the extracting of the ions occur at the same time. 7. A process of purifying polycarbonate comprising: polymerizing a dihydroxy compound and a carbonate source via an interfacial reaction in the presence of a catalyst to form a product mixture comprising an aqueous phase and an organic phase, wherein the organic phase comprises the polycarbonate, the catalyst, ions, and a solvent having a boiling point T b at atmospheric pressure; heating the product mixture to a temperature greater than or equal to the boiling point T b to provide a heated product mixture; separating the aqueous phase and the organic phase of the heated product mixture at a temperature greater than or equal to the boiling point T b to form a separated organic phase and a separated aqueous phase, wherein the separating is by one or both of a separating coalesce and a decanter; extracting the catalyst from the separated organic phase in a first extraction column to form a reduced catalyst organic stream; and extracting the ions from the reduced catalyst organic stream by combining the reduced catalyst organic stream with an aqueous stream in a decanter to form a purified polycarbonate; wherein the separated organic phase, the reduced catalyst organic stream, the aqueous stream, or a combination comprising at least one of the foregoing are at a temperature greater than or equal to the boiling point T b during the extracting the catalyst and the extracting the ions. 8. The process of claim 7 , wherein the separating is by a decanter; and wherein the extracting the ions from the reduced catalyst organic stream by combining the reduced catalyst stream with the aqueous is in a coalescing decanter to form the purified polycarbonate. 9. The process of claim 7 , wherein the separated organic phase, and the reduced catalyst organic stream, and the aqueous stream, are at a temperature greater than or equal to the boiling point T b . 10. The process of claim 7 , further comprising treating the reduced catalyst organic stream in a coalescer before extracting the ions. 11. The process of claim 1 , wherein both the extracting the catalyst and the extracting the ions are by other than a centrifuge. 12. The process of claim 1 , wherein the separating, the extracting the catalyst, and the extracting the ions occur at a temperature greater than or equal to the boiling point T b . 13. The process of claim 1 , wherein the solvent comprises methylene chloride. 14. The process of claim 1 , wherein the temperature is greater than or equal to T b +5° C. 15. The process of claim 1 , wherein the temperature is greater than or equal to T b +20° C. 16. The process of claim 1 , wherein one or both of the extracting the catalyst and the extracting the ions occurs via an extraction column, a separating coalescer, a decanter, or a combination comprising one or more of the foregoing. 17. The process of claim 1 , wherein the polycarbonate comprises a bisphenol A homopolymer, a copolycarbonate comprising bisphenol A carbonate units and bulky bisphenol carbonate units derived from a bisphenol having at least 12 carbon atoms, or a polyestercarbonate comprising bisphenol A carbonate units and terephthalate-isophthalate acid-bisphenol A ester units. 18. The process of claim 17 , wherein the polycarbonate comprises a copolycarbonate comprising bisphenol A carbonate units and 2-phenyl-3,3′-bis(4-hydroxyphenyl) phthalimidine carbonate units, a copolycarbonate comprising bisphenol A carbonate units and 1,1-bis(4-hydroxy-3-methylphenyl)cyclohexane carbonate units, or a copolycarbonate comprising bisphenol A carbonate units and isophorone bisphenol carbonate units. 19. The process of claim 7 , wherein the temperature is greater than or equal to T b +5° C. 20. The process of claim 7 , wherein the temperature is greater than or equal to T b +20° C.
Purifying; Drying · CPC title
Recovery of the polymer · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.