IP Library Granted Patent US 7,910,340
Granted Patent B2
US 7,910,340 · App. 11/981,181 · Granted Mar 22, 2011

Processes for producing coenzyme Q10

Assignee: Kaneka Corporation
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Quick Facts
Patent No.
US 7,910,340
App. No.
11/981,181
Granted
Mar 22, 2011
Kind
B2
Abstract

The present invention relates to a process for producing reduced coenzyme Q 10 which comprises obtaining microbial cells containing reduced coenzyme Q 10 at a ratio of not less than 70 mole % among the entire coenzymes Q 10 , optionally disrupting the cells and recovering thus-produced reduced coenzyme Q 10 . The present invention also relates to a process for producing oxidized coenzyme Q 10 which comprises either recovering oxidized coenzyme Q 10 after oxidizing the above-mentioned microbial cells or disrupted product thereof, or recovering reduced coenzyme Q 10 from the above-mentioned microbial cells or disrupted product thereof to oxidize thus-obtained reduced coenzyme Q 10 thereafter. According to the processes of the present invention, reduced coenzyme Q 10 and oxidized coenzyme Q 10 can be produced simply on the industrial scale.

Claims (65)

1. A process for producing on an industrial scale the oxidized coenzyme Q 10 represented by the following formula:

which comprises culturing reduced coenzyme Q 10 -producing microorganisms in a culture medium containing a carbon source, a nitrogen source, a phosphorus source and a micronutrient to obtain microbial cells containing reduced coenzyme Q 10 at a ratio of not less than 70 mole % among the entire coenzymes Q 10 ,

disrupting the microbial cells to obtain reduced coenzyme Q 10 ; and

oxidizing thus-obtained reduced coenzyme Q 10 to oxidized coenzyme Q 10 and then extracting the oxidized coenzyme Q 10 by an organic solvent under an inert gas atmosphere.

2. The process according to claim 1 ,

wherein the extraction of the oxidized coenzyme Q 10 is carried out by using a hydrophilic organic solvent.

3. The process according to claim 1 ,

wherein the extraction of the oxidized coenzyme Q 10 is carried out by using a hydrophobic organic solvent.

4. The process according to claim 1 , wherein the reduced coenzyme Q 10 is oxidized with an oxidizing agent.

5. The process according to claim 4 , wherein the oxidizing agent is manganese dioxide.

6. The process according to claim 1 , wherein the oxidized coenzyme Q 10 is extracted by a continuous extraction.

7. The process according to claim 6 , wherein the continuous extraction is a countercurrent multistage extraction.

8. The process according to claim 1 , wherein the reduced coenzyme Q 10 upon disrupting has a ratio of not less than 70 mole % among the entire coenzymes Q 10 when measured under the condition that the reduced coenzyme Q 10 is protected from an oxidation reaction.

9. The process according to claim 1 , wherein the inert gas atmosphere comprises nitrogen gas.

10. The process according to claim 1 , wherein the culture medium is at least 750 L.

11. A process for producing on an industrial scale the oxidized coenzyme Q 10 represented by the following formula:

which comprises culturing reduced coenzyme Q 10 -producing microorganisms in a culture medium containing a carbon source, a nitrogen source, a phosphorus source and a micronutrient to obtain microbial cells containing reduced coenzyme Q 10 at a ratio of not less than 70 mole % among the entire coenzymes Q 10 ,

extracting the reduced coenzyme Q 10 by an organic solvent under an inert gas atmosphere, and

oxidizing the extracted reduced coenzyme Q 10 to oxidized coenzyme Q 10 .

12. The process according to claim 11 ,

wherein the extraction of the reduced coenzyme Q 10 is carried out by using a hydrophilic organic solvent.

13. The process according to claim 11 ,

wherein the extraction of the reduced coenzyme Q 10 is carried out by using a hydrophobic organic solvent.

14. The process according to claim 11 , further comprising the step of disrupting the microbial cells.

15. The process according to claim 11 , wherein the reduced coenzyme Q 10 is oxidized with an oxidizing agent.

16. The process according to claim 15 , wherein the oxidizing agent is manganese dioxide.

17. The process according to claim 11 , wherein the reduced coenzyme Q 10 is extracted by a continuous extraction.

18. The process according to claim 17 , wherein the continuous extraction is a countercurrent multistage extraction.

19. The process according to claim 11 , wherein the reduced coenzyme Q 10 upon extracting has a ratio of not less than 70 mole % among the entire coenzymes Q 10 when measured under the condition that the reduced coenzyme Q 10 is protected from an oxidation reaction.

20. The process according to claim 11 , wherein the inert gas atmosphere comprises nitrogen gas.

21. The process according to claim 11 , wherein the culture medium is at least 750 L.

22. A process for producing on an industrial scale the oxidized coenzyme Q 10 represented by the following formula:

which comprises culturing reduced coenzyme Q 10 -producing microorganisms in a culture medium containing a carbon source, a nitrogen source, a phosphorus source and a micronutrient to obtain microbial cells containing reduced coenzyme Q 10 at a ratio of not less than 70 mole % among the entire coenzymes Q 10 ,

disrupting the microbial cells to obtain reduced coenzyme Q 10 ; and

oxidizing thus-obtained reduced coenzyme Q 10 to oxidized coenzyme Q 10 and then extracting the oxidized coenzyme Q 10 by an organic solvent in a sealed tank.

23. The process according to claim 22 ,

wherein the extraction of the oxidized coenzyme Q 10 is carried out by using a hydrophilic organic solvent.

24. The process according to claim 22 ,

wherein the extraction of the oxidized coenzyme Q 10 is carried out by using a hydrophobic organic solvent.

25. The process according to claim 22 , wherein the reduced coenzyme Q 10 is oxidized with an oxidizing agent.

26. The process according to claim 25 , wherein the oxidizing agent is manganese dioxide.

27. The process according to claim 22 , wherein the oxidized coenzyme Q 10 is extracted by a continuous extraction.

28. The process according to claim 27 , wherein the continuous extraction is a countercurrent multistage extraction.

29. The process according to claim 22 , wherein the sealed tank is sealed under an inert gas atmosphere.

30. The process according to claim 29 , wherein the inert gas atmosphere comprises nitrogen gas.

31. The process according to claim 22 , wherein the culture medium is at least 750 L.

32. The process according to claim 22 , wherein the reduced coenzyme Q 10 upon disrupting has a ratio of not less than 70 mole % among the entire coenzymes Q 10 when measured under the condition that the reduced coenzyme Q 10 is protected from an oxidation reaction.

33. A process for producing on an industrial scale the oxidized coenzyme Q 10 represented by the following formula:

which comprises culturing reduced coenzyme Q 10 -producing microorganisms in a culture medium containing a carbon source, a nitrogen source, a phosphorus source and a micronutrient to obtain microbial cells containing reduced coenzyme Q 10 at a ratio of not less than 70 mole % among the entire coenzymes Q 10 ,

extracting the reduced coenzyme Q 10 by an organic solvent in a sealed tank, and

oxidizing the extracted reduced coenzyme Q 10 to oxidized coenzyme Q 10 .

34. The process according to claim 33 ,

wherein the extraction of reduced coenzyme Q 10 is carried out by using a hydrophilic organic solvent.

35. The process according to claim 33 ,

wherein the extraction of the reduced coenzyme Q 10 is carried out by using a hydrophobic organic solvent.

36. The process according to claim 33 , further comprising disrupting the microbial cells.

37. The process according to claim 33 , wherein the reduced coenzyme Q 10 is oxidized with an oxidizing agent.

38. The process according to claim 37 , wherein the oxidizing agent is manganese dioxide.

39. The process according to claim 33 , wherein the reduced coenzyme Q 10 is extracted by a continuous extraction.

40. The process according to claim 39 , wherein the continuous extraction is a countercurrent multistage extraction.

41. The process according to claim 33 , wherein the sealed tank is sealed under a deoxygenized atmosphere.

42. The process according to claim 41 , wherein the deoxygenized atmosphere comprises inert gas.

43. The process according to claim 41 , wherein the deoxygenized atmosphere comprises nitrogen gas.

44. The process according to claim 33 , wherein the culture medium is at least 750 L.

45. The process according to claim 33 , wherein the reduced coenzyme Q 10 upon extracting has a ratio of not less than 70 mole % among the entire coenzymes Q 10 when measured under the condition that the reduced coenzyme Q 10 is protected from an oxidation reaction.

Assignments (2)
CHANGE OF ADDRESS Recorded Jan 15, 2014
From: KANEKA CORPORATION
To: KANEKA CORPORATION
Reel/Frame 032019/0901 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 3, 2011
From: YAJIMA, KAZUYOSHI; KATO, TAKAHISA; KANDA, AKIHISA; KITAMURA, SHIRO; UEDA, YASUYOSHI
To: KANEKA CORPORATION
Reel/Frame 026217/0362 →
Priority Claims (1)
JP 2001-398545 · Dec 27, 2001 · national
Continuity (2)
Division 10500249
Related Publication 20080171373A1 · Jul 17, 2008