IP Library Granted Patent US 7,569,722
Granted Patent B2
US 7,569,722 · App. 11/201,799 · Granted Aug 4, 2009

Process for removal of benzoic acid from an oxidizer purge stream

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Quick Facts
Patent No.
US 7,569,722
App. No.
11/201,799
Granted
Aug 4, 2009
Kind
B2
Abstract

A process is disclosed that relates to the removal of impurities, specifically benzoic acid, from a mother liquor produced in the synthesis of carboxylic acid, typically terephthalic acid.

Claims (27)

1. A process comprising:

(a) subjecting a benzoic acid bearing stream comprising water and benzoic acid to evaporation in an evaporator zone to form a solvent rich vapor and a wash filtrate residue; and

(b) subjecting said solvent rich vapor to distillation in a separation zone to form a solvent rich stream and a benzoic acid rich stream;

 wherein said benzoic acid rich stream comprises at least 15% by weight benzoic acid.

2. The process according to claim 1 wherein said benzoic acid rich stream comprises benzoic acid in an amount greater than 30% by weight.

3. The process according to claim 1 wherein said benzoic acid bearing stream is produced in an aromatic oxidation process.

4. The process according to claim 1 wherein said benzoic acid bearing stream is a vapor stream produced in the oxidation of an aromatic compound.

5. The process according to claim 1 wherein said evaporator zone is operated between about 1 to about 10 atmospheres.

6. A process comprising:

(a) subjecting a benzoic acid bearing stream comprising water and benzoic acid to evaporation in an evaporator zone to form a solvent rich vapor and a wash filtrate residue; and

(b) subjecting said solvent rich vapor to distillation in a separation zone to form a solvent rich stream and a benzoic acid rich stream;

 wherein said benzoic acid rich stream comprises at least 15% by weight benzoic acid; and

(c) recycling at least a portion of the solvent rich stream back to an oxidation reactor in an aromatic oxidation process.

7. The process according to claim 6 wherein said benzoic acid rich stream comprises benzoic acid in an amount greater than 30% by weight.

8. The process according to claim 6 wherein said benzoic acid bearing stream is produced in an aromatic oxidation process.

9. The process according to claim 6 wherein said benzoic acid bearing stream is a vapor stream produced in the oxidation of an aromatic compound.

10. The process according to claim 6 wherein at least 50 wt % of said benzoic acid rich stream is recycled to an oxidation reactor in an aromatic oxidation process.

11. The process according to claim 6 wherein said evaporator zone is operated between about 1 to about 10 atmospheres.

12. A process comprising:

(a) subjecting a benzoic acid bearing stream comprising water and benzoic acid to evaporation in an evaporator zone to form a solvent rich vapor and a wash filtrate residue; wherein said benzoic acid bearing stream is produced in an aromatic oxidation process;

(b) subjecting said solvent rich vapor to distillation in a separation zone to form a solvent rich stream and a benzoic acid rich stream;

 wherein said benzoic acid rich stream comprises from about 5 wt % to about 35 wt % benzoic acid; and

(c) recycling at least 50 wt % of the solvent rich stream to an oxidation reactor in an aromatic oxidation process.

13. The process according to claim 12 wherein said benzoic acid bearing stream is a vapor stream produced in the oxidation of an aromatic compound.

14. The process according to claim 12 wherein at least 75 wt % of said benzoic acid rich stream is recycled to an oxidation reactor in an aromatic oxidation process.

15. The process according to claim 12 wherein said evaporator zone is operated between about 1 to about 10 atmospheres.

16. The process according to claim 12 wherein all of the solvent rich stream is recycled to an oxidation reactor process.

Assignments (3)
CHANGE OF NAME Recorded Jan 11, 2022
From: GRUPO PETROTEMEX, S.A. DE C.V.
To: ALPEK POLYESTER, S.A. DE C.V.
Reel/Frame 058691/0337 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 1, 2011
From: EASTMAN CHEMICAL COMPANY
To: GRUPO PETROTEMEX, S.A. DE C.V.
Reel/Frame 025727/0820 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 10, 2005
From: LIN, ROBERT; GIBSON, PHILIP EDWARD; PARKER, KENNY RANDOLPH
To: EASTMAN CHEMICAL COMPANY
Reel/Frame 017003/0254 →