Method for extracting coenzyme q10 and phospholipid from coenzyme q10 fermentation bacterial powder
US-2020399667-A1 · Dec 24, 2020 · US
US9605009B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9605009-B2 |
| Application number | US-201615092792-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 7, 2016 |
| Priority date | Dec 20, 2012 |
| Publication date | Mar 28, 2017 |
| Grant date | Mar 28, 2017 |
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A method for the purification of lecithin, comprising the steps of: a. reducing the viscosity of lecithin to a viscosity of less than about 10 Pa·s; then b. mixing the lecithin with granulated active carbon; then c. separating the lecithin from the granulated active carbon and recover purified lecithin. Lecithin substantially free of poly-aromatic hydrocarbons, and a food or feed product comprising said lecithin.
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What is claimed is: 1. A method for the purification of lecithin, comprising the steps of: a. reducing the viscosity of lecithin; then b. mixing the lecithin with granulated active carbon; then c. separating the lecithin from the granulated active carbon and recover purified lecithin. 2. A method according to claim 1 , wherein the viscosity of lecithin is reduced by increasing the temperature to about 20° C.-95° C. 3. A method according to claim 1 , wherein the viscosity of lecithin is reduced by mixing the lecithin with a vegetable oil at a temperature of from about 10° C. to about 90° C. 4. A method according to claim 1 , wherein the viscosity of lecithin is reduced by mixing with an organic solvent. 5. A method according to claim 1 , wherein 90 wt % of said granulated active carbon has a diameter of from about 0.2 mm to about 4 mm. 6. A method according to claim 1 , wherein the lecithin and granulated active carbon are mixed at a ratio of from about 0.05% to about 3% by weight of granulated active carbon to lecithin. 7. A method according to claim 1 , wherein the lecithin is separated from the granulated active carbon through gravitational forces. 8. A method according to claim 1 , wherein the lecithin is separated from the granulated active carbon by means of a decanter or a centrifuge. 9. A method according to claim 1 , further comprising the step of: d. filtrating the recovered lecithin. 10. A method according to claim 1 , further comprising the steps of: reducing the viscosity of the recovered purified lecithin by mixing the lecithin with an organic solvent; then removing residual particles or contaminants from the lecithin by means of gravitational forces; then removing the solvent from the lecithin and recovering the lecithin. 11. A method according to claim 1 , further comprising the steps, before step a of claim 1 , of: i. reducing the viscosity of lecithin by mixing the lecithin with an organic solvent; then ii. removing particles or contaminants from the lecithin by means of gravitational forces; then iii. removing the solvent from the lecithin and recover the lecithin.
Fatty acids; Fats; Products containing oils or fats · CPC title
Refining fats or fatty oils · CPC title
Other fatty acid esters, e.g. phosphatides · CPC title
Extraction or purification by physical or chemical treatment of natural phosphatides; Preparation of compositions containing phosphatides of unknown structure · CPC title
Fatty acids or derivatives thereof · CPC title
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