IP Library Granted Patent US 8,076,508
Granted Patent B2
US 8,076,508 · App. 12/315,887 · Granted Dec 13, 2011

Preparation of acetic acid

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Quick Facts
Patent No.
US 8,076,508
App. No.
12/315,887
Granted
Dec 13, 2011
Kind
B2
Abstract

A process for producing acetic acid is disclosed. The process comprises carbonylating methanol to form a reaction mixture and flashing the reaction mixture to form a vapor stream and a liquid stream. The flash tank is equipped with a distillation column. The vapor stream comprises acetic acid and other volatile components but essentially no catalyst. The liquid stream comprises the catalyst and sufficient amounts of water and acetic acid to carry and stabilize the catalyst. The liquid stream is recycled to the carbonylation and the vapor stream is subjected to further separation to produce essentially pure acetic acid.

Claims (32)

1. A process for producing acetic acid, comprising:

(a) carbonylating methanol in the presence of a carbonylation catalyst to form a reaction mixture;

(b) flashing and distilling the reaction mixture in a flash tank equipped with a distillation column to form a liquid stream comprising the catalyst at the bottom of the flash tank and a vapor stream at the top of the distillation column; and

(c) recycling the liquid stream to step (a),

wherein the vapor stream is distilled in a light-ends distillation column to form a bottom stream, a crude acetic acid stream, and an overhead vapor stream,

the overhead vapor stream is condensed and separated into a light phase and a heavy phase, and

a fraction of the light phase is introduced to the top of the flash tank distillation column and a liquid stream is taken from the bottom of the flash tank distillation column and sent to the top of the light-ends distillation column.

2. The process of claim 1 , wherein the flash tank distillation column has at least two trays.

3. The process of claim 1 , wherein the catalyst is selected from the group consisting of rhodium catalysts and iridium catalysts.

4. The process of claim 1 , wherein the catalyst is a rhodium catalyst.

5. The process of claim 1 , wherein the bottom stream is recycled to the carbonylation or to the flash tank.

6. The process of claim 1 , wherein the crude acetic acid stream is distilled in a drying column and in a heavy-ends distillation column to produce purified acetic acid.

7. The process of claim 4 , wherein the catalyst comprises a stabilizer selected from the group consisting of pentavalent Group VA oxides, metal iodide salts, and mixtures thereof.

8. The process of claim 7 , wherein the stabilizer is a phosphine oxide.

9. The process of claim 8 , wherein the stabilizer is triphenylphosphine oxide.

10. The process of claim 7 , wherein the stabilizer is lithium iodide.

11. A process for producing acetic acid, comprising:

(a) carbonylating methanol in the presence of a carbonylation catalyst to form a reaction mixture;

(b) flashing and distilling the reaction mixture in a flash tank equipped with a distillation column to form a liquid stream comprising the catalyst at the bottom of the flash tank and a vapor stream at the top of the distillation column; and

(c) recycling the liquid stream to step (a),

wherein the vapor stream is distilled in a light-ends distillation column to form a bottom stream, a crude acetic acid stream, and an overhead vapor stream,

the overhead vapor stream is condensed and separated into a light phase and a heavy phase, and

a fraction of the crude acetic acid stream is sent to the flash tank distillation column.

12. The process of claim 11 , wherein the flash tank distillation column has at least two trays.

13. The process of claim 11 , wherein the catalyst is selected from the group consisting of rhodium catalysts and iridium catalysts.

14. The process of claim 11 , wherein the bottom stream is recycled to the carbonylation or to the flash tank.

15. The process of claim 11 , wherein the crude acetic acid stream is distilled in a drying column and in a heavy-ends distillation column to produce purified acetic acid.

16. The process of claim 11 , wherein the catalyst is a rhodium catalyst.

17. The process of claim 16 , wherein the catalyst comprises a stabilizer selected from the group consisting of pentavalent Group VA oxides, metal iodide salts, and mixtures thereof.

18. The process of claim 17 , wherein the stabilizer is a phosphine oxide.

19. The process of claim 18 , wherein the stabilizer is triphenylphosphine oxide.

20. The process of claim 17 , wherein the stabilizer is lithium iodide.

Assignments (15)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 033182/0019 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032137/0156 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032123/0799 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: BANK OF AMERICA, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032138/0134 →
APPOINTMENT OF SUCCESSOR ADMINISTRATIVE AGENT Recorded Jan 23, 2014
From: UBS AG, STAMFORD BRANCH
To: BANK OF AMERICA, N.A.
Reel/Frame 032137/0639 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: CITIBANK, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032125/0296 →
SECURITY AGREEMENT Recorded May 19, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 024402/0681 →
SECURITY AGREEMENT Recorded May 18, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 024397/0818 →
SECURITY AGREEMENT Recorded May 7, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 024342/0801 →
SECURITY AGREEMENT Recorded May 6, 2010
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: DEUTSCHE BANK TRUST COMPANY AMERICAS, AS COLLATERAL AGENT
Reel/Frame 024342/0421 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP
Reel/Frame 024337/0285 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP
Reel/Frame 024337/0020 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Nov 10, 2009
From: BRIKO, WAYNE J.; FITZPATRICK, MICHAEL E.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 023530/0467 →
SECURITY AGREEMENT Recorded Oct 30, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 023449/0138 →
SECURITY AGREEMENT Recorded Apr 9, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT
Reel/Frame 022708/0830 →