Preparation of microbial oil

US10633678B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10633678-B2
Application numberUS-201314027588-A
CountryUS
Kind codeB2
Filing dateSep 16, 2013
Priority dateJun 19, 2002
Publication dateApr 28, 2020
Grant dateApr 28, 2020

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The present invention provides a process for the production of a microbial oil comprising culturing a micro-organism in a two stage fermentation process where, in a last stage that precedes the end of fermentation, the carbon source is: consumed by the micro-organisms at a rate greater than it is added to the medium; added at a rate #0.30 M carbon/kg medium; or is rate limiting on the growth of the micro-organism. The micro-organisms thus have the carbon source restricted so that they preferentially metabolise fats or lipids other than arachidonic acid (ARA), so increasing the proportion of ARA in the cells. A microbial oil is then recovered from the micro-organism, using hexane as a solvent, that has at least 50% ARA and at least 90% triglycerides.

First claim

Opening claim text (preview).

We claim: 1. A fermentation process for production of a microbial oil comprising at least 40% arachidonic acid (ARA), the process comprising culturing a microorganism which is Mortierella alpina in a two-stage process in a culture medium inside a fermentation vessel, whereby at a second stage of the fermentation process (a) a carbon source is rate limiting on the growth of the microorganism, (b) the carbon source is restricted such that the microorganism metabolises fat(s) and/or lipid(s) in preference to arachidonic acid (ARA), (c) the carbon source is consumed by the microorganism at a rate greater than it is added to the medium, (d) the carbon source is added at an addition rate of 0.5 g/kg/hr, and (e) the carbon source is controlled so that the concentration of the carbon source is about 5 g/kg of medium about 10 hours before the end of fermentation; whereby the process further comprises extracting the oil from the micro-organism using a non-polar solvent, and wherein the oil has a triglyceride content of at least 90%. 2. The process according to claim 1 , wherein: concentration of the carbon source in the second stage is on average ≤0.17M carbon/kg medium. 3. The process according to claim 1 , wherein fermentation is carried out at a temperature ≥22° C. and ≤30° C. 4. The process according to claim 1 , wherein the carbon source is glucose. 5. The process according to claim 1 , wherein during an earlier stage of fermentation, the carbon source is being added, wherein the earlier stage is prior to the second stage. 6. The process according to claim 5 , wherein during said earlier stage the carbon source is in excess. 7. The process according to claim 1 , wherein cells of the microorganism are pasteurized after fermentation is finished. 8. The process according to claim 1 , wherein the oil comprises at least 50% ARA (wt/wt) based on the oil. 9. The process according to claim 1 , wherein a concentration of the carbon source in said second stage is <4 g/kg of medium. 10. The process according to claim 1 , wherein the solvent is hexane. 11. The process according to claim 8 , wherein: concentration of the carbon source in the second stage is on average ≤0.17 M carbon/kg medium. 12. The process according to claim 8 , wherein fermentation is carried out at a temperature ≥22° C. and ≤30° C. 13. The process according to claim 1 , wherein a concentration of the carbon source in said second stage is <4 g/kg of medium. 14. The process according to claim 8 , wherein the carbon source is glucose. 15. The process according to claim 8 , wherein during an earlier stage of fermentation, the carbon source is being added, wherein the earlier stage is prior to the second stage. 16. The process according to claim 15 , wherein during said earlier stage the carbon source is in excess. 17. The process according to claim 8 , wherein the solvent is hexane. 18. The process according to claim 8 , wherein cells from the microorganism are pasteurized after fermentation is finished.

Assignees

Inventors

Classifications

  • Products or compounds obtained by fermentation, e.g. yoghurt, beer, wine · CPC title

  • Vitamins · CPC title

  • after treatment of microbial biomass not covered by C12N1/02 - C12N1/08 · CPC title

  • of animal origin · CPC title

  • Preparations for care of the skin · CPC title

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What does patent US10633678B2 cover?
The present invention provides a process for the production of a microbial oil comprising culturing a micro-organism in a two stage fermentation process where, in a last stage that precedes the end of fermentation, the carbon source is: consumed by the micro-organisms at a rate greater than it is added to the medium; added at a rate #0.30 M carbon/kg medium; or is rate limiting on the growth of…
Who is the assignee on this patent?
Dsm Ip Assets Bv
What technology area does this patent fall under?
Primary CPC classification C12P7/6472. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Apr 28 2020 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).