IP Library Granted Patent US 7,485,749
Granted Patent B2
US 7,485,749 · App. 11/508,109 · Granted Feb 3, 2009

Preparation of acetic acid

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Quick Facts
Patent No.
US 7,485,749
App. No.
11/508,109
Granted
Feb 3, 2009
Kind
B2
Abstract

A method for removing aldehyde impurities from an acetic acid stream is disclosed. The method comprises reacting aldehyde impurities with a hydroxyl compound in a drying distillation column or a combined column to form corresponding acetals. The acetals are subsequently removed as heavy impurities from acetic acid by distillation.

Claims (38)

1. A method for producing acetic acid, said method comprising:

(a) reacting methanol and carbon monoxide in the presence of a carbonylation catalyst, a catalyst stabilizer, methyl iodide, water and methyl acetate to produce an acetic acid stream comprising acetic acid, water, methyl acetate, methyl iodide, the catalyst, the catalyst stabilizer, and an aldehyde impurity;

(b) flashing at least a portion of the acetic acid stream to produce a vapor stream comprising acetic acid, water, methyl acetate, methyl iodide and the aldehyde impurity, and a liquid stream comprising the catalyst and the catalyst stabilizer;

(c) separating the vapor stream using a distillation column into an acetic acid product stream comprising acetic acid, the aldehyde impurity, and a minor amount of water, and an overhead stream comprising methyl iodide, water, acetic acid, and methyl acetate;

(d) feeding the acetic acid product stream and a hydroxyl compound selected from the group consisting of glycols, glycerin, and C 4-10 alcohols into a distillation column, wherein the aldehyde impurity reacts with the hydroxyl compound to form an acetal, and wherein the water is removed from a top portion of the distillation column and an essentially anhydrous acetic acid product stream comprising acetic acid and the acetal is taken from the distillation column; and

(e) separating the acetal from acetic acid by distillation.

2. The method of claim 1 , wherein the catalyst is a rhodium catalyst.

3. The method of claim 1 , wherein the catalyst stabilizer is selected from the group consisting of pentavalent Group VA oxides, metal iodide salts, and mixtures thereof.

4. The method of claim 1 , wherein the catalyst stabilizer is a phosphine oxide.

5. The method of claim 1 , wherein the catalyst stabilizer is triphenylphosphine oxide.

6. The method of claim 1 , wherein the water concentration in step (a) is 10 wt % or less based on the total weight of the acetic acid stream.

7. The method of claim 1 , wherein the water concentration in step (a) is 6 wt % or less based on the total weight of the acetic acid stream.

8. The method of claim 1 , wherein the hydroxyl compound is a glycol selected from the group consisting of 2-methyl-1,3-propanediol, ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,2-butanediol, 1,3-butanediol, 1,5-pentanediol, 1,6-hexanediol, 2,2-dimethyl-1,3-propanediol, cyclohexane-1,4-dimethanol, neopentyl glycol, and mixtures thereof.

9. The method of claim 1 , wherein the hydroxyl compound is 2-methyl-1,3-propanediol.

10. The method of claim 1 , which comprises recycling the liquid stream of step (b) to the reaction of step (a).

11. The method of claim 1 , which comprises condensing and separating the overhead stream of step (c) in a decanter into a light, aqueous phase comprising water, acetic acid, and methyl acetate, and a heavy, organic phase comprising methyl iodide.

12. The method of claim 11 , wherein the heavy, organic phase is recycled to the reaction of step (a).

13. The method of claim 11 , wherein the light, aqueous phase is recycled to the reaction of step (a) or the distillation of step (c).

14. The method of claim 1 , wherein the aldehyde impurity has a boiling point of 75° C. or higher.

15. The method of claim 1 , wherein the aldehyde impurity is selected from the group consisting of crotonaldehyde, 2-ethylcrotonaldehyde, 2-ethylbutyraldehyde, and mixtures thereof.

16. The method of claim 1 , wherein the aldehyde impurity is crotonaldehyde.

17. The method of claim 1 , wherein in step (d), the reaction of the aldehyde impurity with the hydroxyl compound is performed in the presence of a mineral acid.

18. A method for producing acetic acid, said method comprising:

(a) reacting methanol and carbon monoxide in the presence of a carbonylation catalyst, a catalyst stabilizer, methyl iodide, water and methyl acetate to produce an acetic acid stream comprising acetic acid, water, methyl acetate, methyl iodide, the catalyst, the catalyst stabilizer, and an aldehyde impurity;

(b) flashing at least a portion of the acetic acid stream to produce a vapor stream comprising acetic acid, water, methyl acetate, methyl iodide and the aldehyde impurity, and a liquid stream comprising the catalyst and the catalyst stabilizer;

(c) feeding the vapor stream and a hydroxyl compound selected from the group consisting of glycols, glycerin, and C 4-10 alcohols into a distillation column, wherein the aldehyde impurity reacts with the hydroxyl compound to form an acetal;

(d) withdrawing an essentially anhydrous acetic acid product stream comprising acetic acid and the acetal from the distillation column; and

(e) separating the acetal from acetic acid by distillation.

19. The method of claim 18 , wherein the aldehyde impurity is selected from the group consisting of acetaldehyde, crotonaldehyde, 2-ethylcrotonaldehyde, butyraldehyde, 2-ethylbutyraldehyde, and mixtures thereof.

20. The method of claim 18 , wherein the aldehyde impurity is acetaldehyde.

21. The method of claim 18 , wherein in step (c), the reaction of the aldehyde impurity with the hydroxyl compound is performed in the presence of a mineral acid.

22. A method for producing acetic acid, said method comprising:

(a) reacting methanol and carbon monoxide in the presence of a carbonylation catalyst, a catalyst stabilizer, methyl iodide, water and methyl acetate to produce an acetic acid stream comprising acetic acid, water, methyl acetate, methyl iodide, the catalyst, the catalyst stabilizer, and an aldehyde impurity;

(b) flashing at least a portion of the acetic acid stream to produce a vapor stream comprising acetic acid, water, methyl acetate, methyl iodide and the aldehyde impurity, and a liquid stream comprising the catalyst and the catalyst stabilizer;

(c) feeding the vapor stream and a hydroxyl compound into a distillation column, wherein the aldehyde impurity reacts with the hydroxyl compound selected from the group consisting of glycols, glycerin, and C 4-10 alcohols to form an acetal; and

(d) withdrawing a heavy stream comprising the acetal from the distillation column.

23. The method of claim 22 , which comprises separating the acetal from the heavy stream, disposing the acetal, and recycling the purified heavy stream to the carbonylation of step (a).

24. The method of claim 22 , wherein in step (c), the reaction of the aldehyde impurity with the hydroxyl compound is performed in the presence of a mineral acid.

Assignments (30)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 033182/0019 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 16, 2014
From: MILLENNIUM PETROCHEMICALS INC.
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 033110/0856 →
RELEASE OF SECURITY INTEREST Recorded Jan 30, 2014
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 032097/0234 →
RELEASE OF SECURITY INTEREST Recorded Jan 30, 2014
From: BANK OF AMERICA, N.A.
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 032096/0330 →
APPOINTMENT OF SUCCESSOR ADMINISTRATIVE AGENT Recorded Jan 30, 2014
From: UBS AG, STAMFORD BRANCH
To: BANK OF AMERICA, N.A.
Reel/Frame 032144/0368 →
RELEASE OF SECURITY INTEREST Recorded Jan 30, 2014
From: CITIBANK, N.A.
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 032096/0717 →
RELEASE OF SECURITY INTEREST Recorded Jan 30, 2014
From: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: LYONDELLBASELL ACETYLS, LLC
Reel/Frame 032096/0971 →
RELEASE OF SECURITY INTEREST Recorded Jan 23, 2014
From: CITIBANK, N.A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032125/0296 →
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: 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: DEUTSCHE BANK TRUST COMPANY AMERICAS
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.
Reel/Frame 032123/0799 →
SECURITY AGREEMENT Recorded May 19, 2010
From: LYONDELLBASELL ACETYLS, LLC
To: WELLS FARGO BANK, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 024402/0695 →
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 18, 2010
From: LYONDELLBASELL ACETYLS, LLC
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT
Reel/Frame 024397/0891 →
SECURITY AGREEMENT Recorded May 17, 2010
From: LYONDELLBASELL ACETYLS, LLC
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 024390/0267 →
SECURITY AGREEMENT Recorded May 13, 2010
From: LYONDELLBASELL ACETYLS, LLC
To: DEUTSCHE BANK TRUST COMPANY AMERICAS, AS COLLATERAL AGENT
Reel/Frame 024380/0089 →
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: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0856 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP; MILLENNIUM PETROCHEMICALS, INC.
Reel/Frame 024329/0981 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, LP; MILLENNIUM PETROCHEMICALS, INC.
Reel/Frame 024337/0217 →
RELEASE OF SECURITY INTEREST Recorded May 5, 2010
From: CITIBANK, N.A., AS COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP
Reel/Frame 024337/0705 →
SECURITY AGREEMENT Recorded Oct 30, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.; MILLENNIUM PETROCHEMICALS INC.
To: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
Reel/Frame 023449/0001 →
CORRECTIVE ASSIGNMENT TO CORRECT THE CONVEYING AND RECEIVING PARTIES. PREVIOUSLY RECORDED ON REEL 022542 FRAME 0897. ASSIGNOR(S) HEREBY CONFIRMS THE SECURITY AGREEMENT.. Recorded May 5, 2009
From: LYONDELL CHEMICAL TECHNOLOGY, L.P.; MILLENNIUM PETROCHEMICALS INC.
To: CITIBANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT
Reel/Frame 022634/0262 →
SECURITY AGREEMENT Recorded Apr 15, 2009
From: CITIBANK, N.A., AS ADMINISTRATIVE AGENT AND COLLATERAL AGENT
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; EQUISTAR CHEMICALS, LP; HOUSTON REFINING LP; BASELL USA INC.; MILLENNIUM CHEMICALS INC.; MILLENNIUM PETROCHEMICALS INC.; LYONDELL CHEMICAL COMPANY
Reel/Frame 022542/0897 →
SECURITY AGREEMENT Recorded Aug 4, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; BASELL POLYOLEFIN GMBH; LYONDELL CHEMICAL COMPANY; EQUISTAR CHEMICALS, L.P.
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 021354/0708 →
GRANT OF SECURITY INTEREST IN UNITED STATES PATENTS AND PATENT APPLICATIONS Recorded Mar 26, 2008
From: BASELL POLYOLEFINE GMBH; ARCO CHEMICAL TECHNOLOGY L.P.; ARCO CHEMICAL TECHNOLOGY, INC.; ATLANTIC RICHFIELD COMPANY; BASELL NORTH AMERICA, INC.; EQUISTAR CHEMICALS. LP.; LYONDELL CHEMICAL COMPANY; LYONDELL CHEMICAL TECHNOLOGY, L.P.; LYONDELL PETROCHEMICAL COMPANY; NATIONAL DISTILLERS AND CHEMICAL CORPORATION; OCCIDENTAL CHEMICAL CORPORATION; OLIN CORPORATION; QUANTUM CHEMICAL CORPORATION; BASELL POLYOLEFIN GMBH
To: CITIBANK, N.A., AS COLLATERAL AGENT
Reel/Frame 020704/0562 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 22, 2006
From: SAWYER, GARY A.; BRTKO, WAYNE J.; HANES, RONNIE M.; SALISBURY, BRIAN A.
To: LYONDELL CHEMICAL TECHNOLOGY, L.P.; MILLENNIUM PETROCHEMICALS INC.
Reel/Frame 018228/0690 →