IP Library Granted Patent US 8,802,884
Granted Patent B2
US 8,802,884 · App. 13/706,045 · Granted Aug 12, 2014

Process for producing aromatic carbonates

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Quick Facts
Patent No.
US 8,802,884
App. No.
13/706,045
Granted
Aug 12, 2014
Kind
B2
Abstract

This invention provides a method for producing an alkylaryl carbonate comprising: a) contacting a stream comprising an aromatic hydroxy compound and a stream comprising a dialkylcarbonate in a reactive distillation column containing a bed of heterogeneous transesterification catalyst, the bed having a top and a bottom; and b) withdrawing a product stream comprising the alkylaryl carbonate from the reactive distillation column wherein the aromatic hydroxy compound is fed to the column at a first feed point located above the top of the catalyst bed.

Claims (15)

1. A method for producing an alkylaryl carbonate comprising:

a) contacting a stream comprising an aromatic hydroxy compound and water, and a stream comprising a dialkylcarbonate in a reactive distillation column containing a bed of heterogeneous transesterification catalyst, the bed having a top and a bottom; and

b) withdrawing a product stream comprising the alkylaryl carbonate from the reactive distillation column

wherein the aromatic hydroxy compound is fed to the column at a first feed point located at least one theoretical tray above the top of the catalyst bed; wherein the aromatic hydroxy compound has a water content of less than 0.5 wt % when it first contacts the top of the heterogeneous transesterification catalyst bed.

2. A method as claimed in claim 1 where the reactive distillation column contains an item selected from the group consisting of trays and packing between the top of the catalyst bed and the first feed point.

3. A method as claimed in claim 1 where the reactive distillation column contains a second catalyst bed between the top of the catalyst bed and the first feed point.

4. A method as claimed in claim 3 wherein the second catalyst accelerates the reaction of water with dialkylcarbonate.

5. A method as claimed in claim 1 further comprising feeding a homogeneous transesterification catalyst to the reactive distillation column.

6. A method as claimed in claim 5 wherein the homogeneous transesterification catalyst is fed to the column at a point below the first feed point.

7. A method as claimed in claim 1 wherein the aromatic hydroxy compound is phenol.

8. A method as claimed in claim 1 wherein the dialkylcarbonate is selected from the group consisting of dimethyl carbonate, diethyl carbonate and mixtures thereof.

9. A method as claimed in claim 1 wherein the dialkylcarbonate is fed to the reactive distillation column at a point below the top of the catalyst bed.

10. A method as claimed in claim 1 wherein the dialkylcarbonate is fed to the reactive distillation column at a point below the bottom of the catalyst bed.

11. A method as claimed in claim 1 wherein the heterogeneous catalyst comprises titanium.

12. A method as claimed in claim 1 wherein the aromatic hydroxy compound has a water content of less than 500 ppmw when it first contacts the top of the heterogeneous transesterification catalyst bed.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 13, 2013
From: VAPORCIYAN, GARO GARBIS
To: SHELL OIL COMPANY
Reel/Frame 029804/0157 →