IP Library Granted Patent US 7,102,028
Granted Patent B2
US 7,102,028 · App. 11/139,636 · Granted Sep 5, 2006

Method for producing 3,5-di-tert-butyl-4-hydroxybenzoic acid

Assignee: Kabushiki Kaisha Ueno Seiyaku Oyo Kenkyujo
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Quick Facts
Patent No.
US 7,102,028
App. No.
11/139,636
Granted
Sep 5, 2006
Kind
B2
Abstract

The present invention provides a method for producing 3,5-di-tert-butyl-4-hydroxybenzoic acid comprising: (1) providing 2,6-di-tert-butylphenol which may contain up to 0.5% by weight of 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl; (2) reacting a basic alkali metal compound with an excess amount of the 2,6-di-tert-butylphenol, which is in excess of the basic alkali metal compound, to give the alkali metal 2,6-di-tert-butylphenolate; and (3) reacting the alkali metal 2,6-di-tert-butylphenolate obtained in step (2) with carbon dioxide to give 3,5-di-tert-butyl-4-hydroxybenzoic acid. According to the method of the present invention, 3,5-di-tert-butyl-4-hydroxybenzoic acid can be obtained with high and stable yield.

Claims (21)

1. A method for producing 3,5-di-tert-butyl-4-hydroxybenzoic acid comprising:

(1) providing 2,6-di-tert-butylphenol which may contain up to 0.5% by weight of 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl;

(2) reacting sodium methoxide with an excess amount of the 2,6-di-tert-butylphenol, which is excess of sodium methoxide, to give sodium 2,6-di-tert-butylphenolate; and

(3) reacting the sodium 2,6-di-tert-butylphenolate obtained in step (2) with carbon dioxide to give 3,5-di-tert-butyl-4-hydroxybenzoic acid.

2. The method according to claim 1 , wherein step (1) comprises purifying 2,6-di-tert-butylphenol so that the 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl content in 2,6-di-tert-butylphenol is no more than 0.5% by weight.

3. The method according to claim 1 , wherein the 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl content in 2,6-di-tert-butylphenol is no more than 0.3% by weight.

4. The method according to claim 2 , wherein 2,6-di-tert-butylphenol is purified so that the 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl content in 2,6-di-tert-butylphenol is no more than 0.3% by weight.

5. The method according to claim 1 , wherein in step (2) sodium methoxide and 2,6-di-tert-butylphenol are reacted at a temperature of 80–300° C. and at the same time alcohol, which is generated as byproduct, is distilled away from the reaction.

6. The method according to claim 1 , wherein the starting amount of 2,6-di-tert-butylphenol is 2–30 fold moles to sodium methoxide.

7. The method according to claim 2 , wherein 2,6-di-tert-butylphenol is subjected to distillation under reduced pressure at a temperature of 80–200° C.

8. A method for producing 3,5-di-tert-butyl-4-hydroxybenzoic acid comprising:

(a) reacting sodium methoxide with an excess amount of 2,6-di-tert-butylphenol, which is in excess of sodium methoxide, to give sodium 2,6-di-tert-butylphenolate;

(b) reacting the sodium 2,6-di-tert-butylphenolate obtained in step (a) with carbon dioxide to give 3,5-di-tert-butyl-4-hydroxybenzoic acid;

(c) collecting unreacted 2,6-di-tert-butylphenol from the reaction system after step (b);

(d) purifying 2,6-di-tert-butylphenol collected in step (c) so that the 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl content in 2,6-di-tert-butylphenol is no more than 0.5% by weight; and

(e) conducting steps (a)–(d) repeatedly using the 2,6-di-tert-butylphenol purified in step (d) for step (a) of the next cycle.

9. The method according to claim 8 , wherein in step (d) 2,6-di-tert-butylphenol is purified so that the 3,3′,5,5′-tetra-tert-butyl-4,4′-dihydroxybiphenyl content in 2,6-di-tert-butylphenol is no more than 0.3% by weight.

10. The method according to claim 8 , wherein in step (a) sodium methoxide and 2,6-di-tert-butylphenol are reacted at a temperature of 80–300° C. and at the same time alcohol, which is generated as byproduct, is distilled away from the reaction.

11. The method according to claim 8 , wherein the starting amount of 2,6-di-tert-butylphenol is 2–30 fold moles to sodium methoxide.

12. The method according to claim 8 , wherein in step (d) 2,6-di-tert-butylphenol is subjected to distillation under reduced pressure at a temperature of 80–200° C.

13. The method according to claim 8 , wherein the steps (a)–(d) are repeatedly conducted no less than five times.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 22, 2008
From: UENO TECHNOLOGY CO., LTD.
To: UENO FINE CHEMICALS INDUSTRY, LTD.
Reel/Frame 021561/0559 →
CHANGE OF NAME Recorded Sep 12, 2008
From: KABUSHIKI KAISHA UENO SEIYAKU OYO KENKYUJO
To: UENO TECHNOLOGY CO., LTD.
Reel/Frame 021523/0034 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 10, 2005
From: OTSUKA, RYOICHI
To: KABUSHIKI KAISHA UENO SEIYAKU OYO KENKYUJO
Reel/Frame 016881/0880 →
Priority Claims (1)
JP 2004-158968 · May 28, 2004 · national
Continuity (1)
Related Publication 20050267311A1 · Dec 1, 2005