IP Library Granted Patent US 7,671,165
Granted Patent B2
US 7,671,165 · App. 12/122,234 · Granted Mar 2, 2010

Method of forming polycarbonate

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Quick Facts
Patent No.
US 7,671,165
App. No.
12/122,234
Granted
Mar 2, 2010
Kind
B2
Abstract

A method of forming polycarbonate includes the steps of introducing a plurality of reaction components to a reactor operating under melt polymerization conditions and removing ester-substituted phenol from the reactor. The plurality of reaction components include a dihydroxy compound, an ester-substituted diaryl carbonate, and a melt transesterification catalyst. The reaction components are introduced in a plurality of reaction component streams. A first reaction component streams includes a melt transesterification catalyst dissolved or suspended in a liquid carrier containing an ester-substituted phenol. The composition of the first reaction component stream is selected such that ester-substituted phenol is not generated as a reaction product in the first reaction component stream.

Claims (46)

1. A method of forming polycarbonate comprising the steps of:

(I) introducing a plurality of reaction components to a reactor operating under melt polymerization conditions, the plurality of reaction components comprising a dihydroxy compound, an ester-substituted diaryl carbonate, and a melt transesterification catalyst, wherein:

the reaction components are introduced in a plurality of reaction component streams,

a first reaction component streams comprises a melt transesterification catalyst dissolved or suspended in a liquid carrier comprising an ester-substituted phenol, wherein the composition of the first reaction component stream is selected such that ester-substituted phenol is not generated as a reaction product in the first reaction component stream, and

(II) removing ester-substituted phenol from the reactor, thereby allowing the reaction components to react to form polycarbonate.

2. The method of claim 1 , wherein the first reaction component stream comprises between 0.0001 and 3.0000 wt. % catalyst and between 97.0000 wt. % and 99.9999 wt. % ester-substituted phenol.

3. The method of claim 1 , wherein the first reaction component stream further comprises a polar protic co-solvent.

4. The method of claim 3 , wherein the polar protic co-solvent is present in a ratio of 0.1 to 50.0 wt % polar protic co-solvent to 50.0 to 99.9 wt % ester-substituted phenol.

5. The method of claim 3 , wherein the polar protic co-solvent is selected from the group consisting of methanol, ethanol, formic acid, and acetic acid.

6. The method of claim 1 , wherein the reaction components in the first reaction component stream further comprise a dihydroxy compound.

7. The method of claim 6 , wherein the first reaction component stream comprises between 0.0001 and 3.0000 wt. % catalyst, between 1.0000 and 10.0000 wt. % dihydroxy compound, and between 87.0000 and 98.9999 wt. % ester-substituted phenol.

8. The method of claim 1 , wherein the reaction components in the first reaction component stream further comprise an ester-substituted diaryl carbonate.

9. The method of claim 8 , wherein the first reaction component stream comprises between 0.0001 and 3.0000 wt. % catalyst, between 1.0000 and 50.0000 wt. % ester-substituted diaryl carbonate, and between 47.0000 and 98.9999 wt. % ester-substituted phenol.

10. The method of claim 1 , wherein the ester-substituted diaryl carbonate comprises bismethylsalicylcarbonate and the ester-substituted phenol comprises methyl salicylate.

11. The method of claim 1 , wherein a second reaction component streams comprises an ester-substituted diaryl carbonate, a dihydroxy compound, or both an ester-substituted diaryl carbonate and a dihydroxy compound dissolved or suspended in a carrier liquid comprising an ester-substituted phenol, wherein the composition of the second reaction component stream is selected such that ester-substituted phenol is not generated as a reaction product in the second reaction component stream.

12. The method of claim 11 , wherein the reaction components in the first reaction component stream comprise a melt transesterification catalyst and a dihydroxy compound, and wherein the reaction component in the second reaction component stream comprises an ester-substituted diaryl carbonate.

13. The method of claim 11 , wherein the reaction components in the first reaction component stream comprise a melt transesterification catalyst and an ester-substituted diaryl carbonate, and wherein the reaction component in the second reaction component stream comprises a dihydroxy compound.

14. The method of claim 11 , wherein the reaction component in the first reaction component stream comprises a melt transesterification catalyst and wherein the reaction components in the second reaction component stream comprise a dihydroxy compound and an ester-substituted diaryl carbonate.

15. The method of claim 1 , wherein the method further comprises the step of:

introducing a reaction agent additive stream to the plurality of reaction components in the reactor, wherein the additive stream comprises a reaction agent additive dissolved or suspended in an ester-substituted phenol.

16. The method of claim 15 , wherein the reaction agent additive is selected from the group consisting of antioxidants, branching agents, and end-capping agents.

17. The method of claim 1 , wherein the method further comprises the steps of:

introducing a processing agent additive stream to the polycarbonate, wherein the processing agent additive stream comprises a processing agent additive dissolved or suspended in an ester-substituted phenol,

and blending the polycarbonate with the processing agent additive to produce a polycarbonate further comprising a processing agent additive.

18. The method of claim 17 , wherein the processing agent additive is selected from the group consisting of impact modifiers, colorants, mold release agents, fire retardants, and UV stabilizers.

19. A method of forming polycarbonate comprising the steps of:

(I) introducing a plurality of reaction components to a reactor operating under melt polymerization conditions, the plurality of reaction components comprising a dihydroxy compound, an ester-substituted diaryl carbonate, and a melt transesterification catalyst, wherein:

the reaction components are introduced in a plurality of reaction component streams,

a first reaction component streams comprises an ester-substituted diaryl carbonate, a dihydroxy compound, or both an ester-substituted diaryl carbonate and a dihydroxy compound dissolved or suspended in a carrier liquid comprising an ester-substituted phenol, wherein the composition of the first reaction component stream is selected such that ester-substituted phenol is not generated as a reaction product in the first reaction component stream, and

(II) removing ester-substituted phenol from the reactor, thereby allowing the reaction components to react to form polycarbonate.

20. The method of claim 19 , wherein the reaction components further comprise a polycarbonate oligomer.

21. The method of claim 19 , wherein the reaction component in the first reaction component stream comprises a dihydroxy compound.

22. The method of claim 21 , wherein the first reaction component stream comprises between 1.0 wt. % and 10.0 wt. % dihydroxy compound, and between 90.0 wt. % and 99.0 wt. % ester-substituted phenol.

23. The method of claim 21 , wherein the reaction components in the first reaction component stream further comprises a ester-substituted diaryl carbonate.

24. The method of claim 23 , wherein the first reaction component stream comprises between 1.0 wt. % and 10.0 wt. % dihydroxy compound, between 1.0 and 50.0 wt. % ester-substituted diaryl carbonate, and between 40.0 wt. % and 98.0 wt. % ester-substituted phenol.

25. The method of claim 19 , wherein the reaction component in the first reaction component stream comprises an ester-substituted diaryl carbonate.

26. The method of claim 25 , wherein the first reaction component stream comprises between 1.0 and 50.0 wt. % ester-substituted diaryl carbonate, and between 50.0 wt. % and 99.0 wt. % ester-substituted phenol.

27. The method of claim 19 , wherein the method further comprises the step of:

introducing a reaction agent additive stream to the plurality of reaction components in the reactor, wherein the reaction agent additive stream comprises a reaction agent additive dissolved or suspended in an ester-substituted phenol.

28. The method of claim 19 , wherein the method further comprises the steps of:

introducing a processing agent additive stream to the polycarbonate, wherein the processing agent additive stream comprises a processing agent additive dissolved or suspended in an ester-substituted phenol,

and blending the polycarbonate with the processing agent additive to produce a polycarbonate further comprising a processing agent additive.

29. A method of forming polycarbonate comprising the steps of:

(I) introducing a plurality of reaction components to a reactor operating under melt polymerization conditions, the plurality of reaction components comprising a dihydroxy compound, an ester-substituted diaryl carbonate, and a melt transesterification catalyst,

(II) introducing a reaction agent additive stream to the plurality of reaction components in the reactor, wherein the reaction agent additive stream comprises a reaction agent additive dissolved or suspended in an ester-substituted phenol, and

(III) removing ester-substituted phenol from the reactor, thereby allowing the reaction components to react to form polycarbonate.

Assignments (5)
CORRECTIVE ASSIGNMENT TO CORRECT THE REMOVE THE APPLICATION NUMBER 15039474 PREVIOUSLY RECORDED AT REEL: 054528 FRAME: 0467. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Mar 23, 2021
From: SABIC GLOBAL TECHNOLOGIES B.V.
To: SHPP GLOBAL TECHNOLOGIES B.V.
Reel/Frame 057453/0680 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 26, 2020
From: SABIC GLOBAL TECHNOLOGIES B.V.
To: SHPP GLOBAL TECHNOLOGIES B.V.
Reel/Frame 054528/0467 →
CHANGE OF NAME Recorded Jun 12, 2017
From: SABIC INNOVATIVE PLASTICS IP B.V
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 042768/0323 →
RELEASE OF SECURITY INTEREST Recorded Mar 17, 2014
From: CITIBANK, N.A.
To: SABIC INNOVATIVE PLASTICS IP B.V.
Reel/Frame 032459/0798 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 26, 2008
From: BRACK, HANS-PETER; DAVIS, PETER K.; DOMINGO FUSTER, DAVID; GARCIA AGUDO, JORGE; HIDALGO LLINAS, GERARDO; SALOMON CHELIZ, MIGUEL ANGEL; VIC FERNANDEZ, IGNACIO; VAN DER WEKKE, LAURUS; WILLEMSE, DENNIS JAMES PATRICK MARIA
To: SABIC INNOVATIVE PLASTICS IP BV
Reel/Frame 021157/0021 →