Process for purification of diphenyl carbonate for the manufacturing of high quality polycarbonate

Patent metadata

Field	Value
Publication number	US-9732028-B2
Application number	US-201414206692-A
Country	US
Kind code	B2
Filing date	Mar 12, 2014
Priority date	Mar 15, 2013
Publication date	Aug 15, 2017
Grant date	Aug 15, 2017

Abstract

A process for purifying a diaryl carbonate, comprises introducing an aqueous stream to a diaryl carbonate stream that comprises a metal contaminant, wherein the aqueous stream reacts with the metal contaminant to form a precipitate; wherein introducing the aqueous stream to the diaryl carbonate stream results in introducing 100 to 10,000 ppm water based on the total composition of the diaryl carbonate stream and the aqueous stream; removing the precipitate via one or both of a separation column and a filter to result in a purified diaryl carbonate.

First claim

We claim:

1. A process for purifying a diaryl carbonate, comprising:
reacting an aromatic hydroxy compound with a dialkyl carbonate in the presence of a transesterification catalyst to form the diaryl carbonate;
introducing an aqueous stream to a molten stream that comprises the diaryl carbonate and a metal contaminant, wherein the molten stream comprises greater than or equal to 90 wt % of the diaryl carbonate based on the total weight of the molten stream, wherein the introducing occurs at a temperature of 120° C. to 250° C., wherein the aqueous stream reacts with the metal contaminant to form a precipitate; wherein introducing the aqueous stream to the molten stream results in introducing 100 to 8,000 ppm water based on the total composition of the molten stream;
removing the precipitate via one or both of a separation column and a filter to result in a purified diaryl carbonate;
wherein when the removing utilizes the separation column, the process further comprises:
removing a bottom stream comprising the precipitate from the separation column;
removing a top stream from the separation column;
directing a top stream first portion into the separation column and collecting a top stream second portion, wherein the top stream second portion comprises the purified diaryl carbonate.

2. The process of claim 1 , wherein the removing utilizes the separation column, and wherein the introducing occurs before the molten stream enters the separation column.

3. The process of claim 1 , wherein the removing utilizes the separation column, and wherein the introducing occurs before the top stream first portion is directed into the separation column.

4. The process of claim 1 , wherein the removing utilizes the filter.

5. The process of claim 1 , wherein the metal contaminant comprises titanium, lead, tin, zirconium, molybdenum, niobium, vanadium, iron, zinc, aluminum, yttrium, lanthanum, hafnium, tungsten, neodymium, samarium, ytterbium, copper, chromium, nickel, manganese, bismuth, or a combination comprising one or more of the foregoing.

6. The process of claim 1 , wherein greater than or equal to 90 wt % of the metal contaminant is removed based on the total weight of the metal contaminant present in the molten stream.

7. The process of claim 1 , wherein the aromatic hydroxy compound has the formula (III)

wherein n is an integer from 1 to 3 and each R 2 is independently a C 1-34 alkyl, a C 1-34 alkoxy, a C 5-34 cycloalkyl, a C 7-34 alkylaryl, a C 6-34 aryl, a halogen radical, or —COO—R′, wherein R′ is H, a C 1-34 alkyl, C 1-34 alkoxy, C 5-34 cycloalkyl, C 7-34 alkylaryl, or C 6-34 aryl.

8. The process of claim 1 , wherein the diaryl carbonate has the formula (I)

wherein n is an integer from 1 to 3 and each R 2 is independently, a C 1-34 alkyl, a C 1-34 alkoxy, a C 5-34 cycloalkyl, a C 7-34 alkylaryl; a C 6-34 aryl; a halogen radical, or —COO—R′, wherein R′ is H, a C 1-34 alkyl, a C 1-34 alkoxy, a C 5-34 cycloalkyl, a C 7-34 alkylaryl; or a C 6-34 aryl.

9. The process of claim 1 , wherein the introducing occurs in a mixing device.

10. The process of claim 1 , wherein the aromatic hydroxy compound is phenol and the diaryl carbonate is diphenyl carbonate; wherein the molten stream comprises greater than or equal to 99 wt % diphenyl carbonate based on the total weight of the molten stream.

11. The process of claim 1 , wherein the purified diaryl carbonate comprises less than or equal to 38 ppb of molybdenum; less than or equal to 38 ppb of vanadium; less than or equal to 38 ppb of chromium; less than or equal to 85 ppb of titanium; less than or equal to 425 ppb of niobium; less than or equal to 38 ppb of nickel; less than or equal to 12 ppb of zirconium; less than or equal to 12 ppb of iron, or a combination comprising one or more of the foregoing based on a total weight of the purified diaryl carbonate.

12. The process of claim 10 , wherein the purified diaryl carbonate comprises less than or equal to 38 ppb of molybdenum; less than or equal to 38 ppb of vanadium; less than or equal to 38 ppb of chromium; less than or equal to 85 ppb of titanium; less than or equal to 425 ppb of niobium; less than or equal to 38 ppb of nickel; less than or equal to 12 ppb of zirconium; less than or equal to 12 ppb of iron, or a combination comprising one or more of the foregoing based on a total weight of the purified diaryl carbonate.

13. The process of claim 10 , wherein the metal contaminant comprises iron and titanium.

Assignees

• Sabic Global Technologies Bv

Inventors

• Fernandez Ignacio Vic
• Lyakhovych Mykhaylo
• Nadal Sergio Ferrer

Classifications

• C02F1/52

  by flocculation or precipitation of suspended impurities {(C02F1/463 takes precedence)} · CPC title

• C02F1/04

  by distillation or evaporation · CPC title

• C02F2101/22

  Chromium or chromium compounds, e.g. chromates · CPC title

• C02F2101/206

  Manganese or manganese compounds · CPC title

• C02F1/62

  Heavy metal compounds · CPC title