Process for making ethanol by fermentation
US-2017002383-A1 · Jan 5, 2017 · US
US11725221B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11725221-B2 |
| Application number | US-201816636940-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 9, 2018 |
| Priority date | Aug 10, 2017 |
| Publication date | Aug 15, 2023 |
| Grant date | Aug 15, 2023 |
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This invention relates to a method of using a two-step serial centrifugation process in extracting nutritive oil from a fermentation broth, this novel method prevents oil yield losses while preserving product quality.
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What is claimed is: 1. A method of improving product yield of a polyunsaturated fatty acid (PUFA) oil containing product, wherein the method comprises: (a) directing a PUFA oil-containing fermentation broth to a first centrifuge and subjecting the PUFA oil-containing fermentation broth to a first centrifugation step within the first centrifuge to form a first centrifuged product comprised of a first light phase and a first heavy phase; (b) separating the first light phase from the first heavy phase in the first centrifuged product by making a first separation cut of the first centrifuged product into the first heavy phase below an interface between the first light phase and the first heavy phase thereof; (c) discarding the first heavy phase separated from the first centrifuged product and directing the first light phase separated from the first centrifuged product to a second centrifuge; (d) subjecting the first light phase separated from the first centrifuged product to a second centrifugation step in the second centrifuge to form a second centrifuged product comprised of a second light phase and a second heavy phase; (e) separating the second light phase from the second heavy phase in the second centrifuged product by making a second separation cut of the second centrifuged product in the second light phase close to an interface between the second light phase and the second heavy phase thereof; (f) retaining the second light phase separated from the second centrifuged product and recycling the second heavy phase obtained from the second centrifuged product to fresh PUFA oil-containing fermentation broth to be directed to the first centrifuge. 2. The method of claim 1 , wherein the PUFA oil yield of the second light phase is greater than 88%. 3. The method according to claim 1 , wherein step (a) comprises the steps of: (a1) adding the fermentation broth to a vessel; (a2) adding a component to the fermentation broth to facilitate breaking of emulsion formation; (a3) heating the vessel; and (a4) pumping the fermentation broth to a first centrifuge. 4. The method of claim 3 , wherein the component in step (a2) is an enzyme or sodium hydroxide. 5. The method of claim 4 , wherein in step (a3) comprises heating the vessel to a temperature selected from the group consisting of at least 40° C., at least 50° C., at least 60° C., at least 70° C., at least 75° C., at least 80° C., at least 85° C., at least 90° C., and at least 95° C. 6. The method of claim 3 , wherein PUFA oil yield of the second light phase is greater than 88%. 7. The method of claim 6 , wherein PUFA oil yield of the second light phase is greater than 92%. 8. The method of claim 6 , wherein PUFA oil yield of the second light phase is greater than 95%. 9. The method according to claim 3 , wherein step (c) comprises the step of pumping the first light phase from the first centrifuge into the second centrifuge. 10. The method of claim 1 , wherein the process comprises repeating the steps (a)-(f) at least one time. 11. The method of claim 10 , wherein the process comprises repeating the steps (a)-(f) two more times. 12. The method of claim 10 , wherein the process comprises repeating the steps (a)-(f) three more times.
containing polyunsaturated fatty acid [PUFA] residues, i.e. having two or more double bonds in their backbone · CPC title
Working-up · CPC title
Fatty acids or derivatives thereof · CPC title
by using a centrifuge · CPC title
by extracting · CPC title
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