Method of preparing a purified ester-substituted phenol stream
View Patent ↗A method of producing a purified ester-substituted phenol stream is provided. The method includes a first step of obtaining from a melt transesterification reaction a byproduct stream containing a residual ester-substituted diaryl carbonate, an ester-substituted phenol, a residual melt transesterification catalyst, and a catalyst degradation product. A second step includes treating the reaction byproduct stream to separate ester-substituted phenol and catalyst degradation product from residual ester-substituted diaryl carbonate and residual melt transesterification catalyst to create a light recycle stream containing ester-substituted phenol and catalyst degradation product and a heavy recycle stream containing residual ester-substituted diaryl carbonate and residual melt transesterification catalyst. A third step includes treating the light recycle stream to reduce catalyst degradation product concentration thereby producing a purified ester-substituted phenol stream.
1. A method of producing a purified ester-substituted phenol stream from a melt transesterification reaction byproduct stream, the method comprising the sequential steps of:
(a) obtaining from a melt transesterification reaction a byproduct stream comprising a residual ester-substituted diaryl carbonate, an ester-substituted phenol, a residual melt transesterification catalyst, and a catalyst degradation product,
wherein the melt transesterification catalyst comprises a tetraalkyl phosphonium hydroxide, a tetraalkyl ammonium hydroxide, or both, wherein at least one alkyl group of the tetraalkyl phosphonium hydroxide, the tetraalkyl ammonium hydroxide, or both, is a methyl group, and
wherein the catalyst degradation product comprises a trialkyl phosphine, a trialkyl amine, or both,
(b) treating the byproduct stream to separate ester-substituted phenol and catalyst degradation product from residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, thereby creating a light recycle stream comprising ester-substituted phenol and catalyst degradation product and a heavy recycle stream comprising residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, and
(c) treating the light recycle stream to reduce catalyst degradation product concentration,
thereby producing a purified ester-substituted phenol stream.
2. The method of claim 1 , wherein step (b) is accomplished using a first rectification tower.
3. The method of claim 2 , wherein step (c) is accomplished using a second rectification tower.
4. The method of claim 2 , wherein step (c) is accomplished by washing the light recycle stream with an aqueous solution.
5. The method of claim 2 , wherein step (c) is accomplished by mixing the light recycle stream with an ester-substituted phenol stream containing a lower concentration of the catalyst degradation product than the light recycle stream.
6. The method of claim 1 , wherein the light recycle stream further comprises residual melt transesterification catalyst in an amount of less than 0.10 ppm.
7. The method of claim 1 , wherein the purified ester-substituted phenol stream comprises less than 0.10 ppm of catalyst degradation product.
8. The method of claim 1 , wherein:
the tetraalkyl phosphonium hydroxide comprises tetramethyl phosphonium hydroxide, diethyldimethyl phosphonium hydroxide, or both,
the tetraalkyl ammonium hydroxide comprises tetramethyl ammonium hydroxide, diethyldimethyl ammonium hydroxide, or both, and
the catalyst degradation product is trimethyl phosphine, diethylmethyl phosphine, dimethylethyl phosphine, trimethyl amine, diethylmethyl amine, dimethylethyl amine, or any combination thereof.
9. The method of claim 1 , wherein the byproduct stream further comprises a residual dihydroxy monomer compound and a dihydroxy monomer degradation product, wherein step (b) is performed to create a light recycle stream further comprising dihydroxy monomer degradation product and a heavy recycle stream further comprising residual dihydroxy monomer compound, and wherein step (c) is performed to reduce catalyst degradation product concentration and dihydroxy monomer degradation product concentration in the light recycle stream.
10. The method of claim 9 , wherein the purified ester-substituted phenol stream comprises less than 100 ppm dihydroxy monomer degradation product.
11. A method of producing a purified ester-substituted phenol stream from a melt transesterification reaction byproduct stream, the method comprising the sequential steps of:
(a) obtaining from a melt transesterification reaction a byproduct stream comprising a residual ester-substituted diaryl carbonate, an ester-substituted phenol, a residual melt transesterification catalyst, and a catalyst degradation product,
wherein the melt transesterification catalyst comprises a tetraalkyl phosphonium hydroxide, a tetraalkyl ammonium hydroxide, or both, wherein at least one alkyl group of the tetraalkyl phosphonium hydroxide, the tetraalkyl ammonium hydroxide, or both, is a methyl group, and
wherein the catalyst degradation product comprises a trialkyl phosphine, a trialkyl amine, or both,
(b) introducing the byproduct stream to a first rectification column operating under conditions to separate ester-substituted phenol and catalyst degradation product from residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, thereby creating a light recycle stream comprising ester-substituted phenol and catalyst degradation product and a heavy recycle stream comprising residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, and
(c) introducing the light recycle stream to a second rectification column operating under conditions to separate catalyst degradation product from ester-substituted phenol, thereby creating a catalyst degradation product stream and a purified ester-substituted phenol stream, wherein the ester-substituted phenol stream has less than 1.00 ppm catalyst degradation product present.
12. The method of claim 11 , wherein the light recycle stream further comprises residual melt transesterification catalyst in an amount of less than 0.10 ppm.
13. The method of claim 1 , wherein the purified ester-substituted phenol stream phenol comprises less than 0.10 ppm of catalyst degradation product.
14. The method of claim 11 , wherein:
the tetraalkyl phosphonium hydroxide comprises tetramethyl phosphonium hydroxide, diethyldimethyl phosphonium hydroxide, or both,
the tetraalkyl ammonium hydroxide comprises tetramethyl ammonium hydroxide, diethyldimethyl ammonium hydroxide, or both, and
the catalyst degradation product is trimethyl phosphine, diethylmethyl phosphine, dimethylethyl phosphine, trimethyl amine, diethylmethyl amine, dimethylethyl amine, or any combination thereof.
15. The method of claim 11 , wherein the method further comprises the step of:
(d) introducing the purified ester-substituted phenol stream to a single-stage separator.
16. The method of claim 11 , wherein the byproduct stream further comprises a residual dihydroxy monomer compound and a dihydroxy monomer degradation product, step (b) is performed to create a light recycle stream further comprising dihydroxy monomer degradation product and a heavy recycle stream further comprising residual dihydroxy monomer compound, and step (c) is performed to produce a catalyst degradation product stream further comprising dihydroxy monomer degradation product and a purified ester-substituted phenol stream, wherein the ester-substituted phenol stream has less than 1.00 ppm catalyst degradation product present and less than 100 ppm dihydroxy monomer degradation product present.
17. A method of producing an ester-substituted diaryl carbonate from a purified ester-substituted phenol stream from a melt transesterification reaction byproduct stream, the method comprising the sequential steps of:
(a) obtaining from a melt transesterification reaction a byproduct stream comprising a residual ester-substituted diaryl carbonate, an ester-substituted phenol, a residual melt transesterification catalyst, and a catalyst degradation product,
wherein the melt transesterification catalyst comprises a tetraalkyl phosphonium hydroxide, a tetraalkyl ammonium hydroxide, or both, wherein at least one alkyl group of the tetraalkyl phosphonium hydroxide, the tetraalkyl ammonium hydroxide, or both, is a methyl group, and
wherein the catalyst degradation product comprises a trialkyl phosphine, a trialkyl amine, or both,
(b) introducing the byproduct stream to a first rectification column operating under conditions to separate ester-substituted phenol and catalyst degradation product from residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, thereby creating a light recycle stream comprising ester-substituted phenol and catalyst degradation product and a heavy recycle stream comprising residual ester-substituted diaryl carbonate and residual melt transesterification catalyst, and
(c) introducing the light recycle stream to a second rectification column operating under conditions to separate catalyst degradation product from ester-substituted phenol, thereby creating a catalyst degradation product stream and a purified ester-substituted phenol stream, wherein the ester-substituted phenol stream has less than 1.00 ppm catalyst degradation product present,
(d) contacting the ester-substituted phenol stream with phosgene under conditions sufficient to form ester-substituted diaryl carbonate,
thereby forming ester-substituted diaryl carbonate.
18. The method of claim 17 , wherein the light recycle stream further comprises melt transesterification catalyst in an amount of less than 0.10 ppm.
19. The method of claim 17 , wherein the purified ester-substituted phenol stream comprises less than 0.10 ppm of catalyst degradation product.
20. The method of claim 17 , wherein:
the tetraalkyl phosphonium hydroxide comprises tetramethyl phosphonium hydroxide, diethyldimethyl phosphonium hydroxide, or both,
the tetraalkyl ammonium hydroxide comprises tetramethyl ammonium hydroxide, diethyldimethyl ammonium hydroxide, or both, and
the catalyst degradation product is trimethyl phosphine, diethylmethyl phosphine, dimethylethyl phosphine, trimethyl amine, diethylmethyl amine, dimethylethyl amine, or any combination thereof.