Feedstuff of high abrasion resistance and good stability in water, containing pufas
US-2017295823-A1 · Oct 19, 2017 · US
US11946017B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11946017-B2 |
| Application number | US-201716317305-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 12, 2017 |
| Priority date | Jul 13, 2016 |
| Publication date | Apr 2, 2024 |
| Grant date | Apr 2, 2024 |
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The current invention relates to a method of separating polyunsaturated fatty acids containing lipids from a lipids containing biomass.
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The invention claimed is: 1. A method of separating a polyunsaturated fatty acids (PUFAs)-containing lipid from the debris of a biomass, comprising the following steps: a) providing a suspension of a biomass comprising cells which contain a PUFAs-containing lipid; b) lysing the cells of the biomass; c) heating the suspension obtained in step b) to a temperature of 80° C. to 100° C., and adjusting the pH to a value of 9.0 to 11.5; d) maintaining the temperature and pH value in the ranges of paragraph c) for at least 10 hours thereby forming a demulsified suspension; e) harvesting the PUFAs-containing oil by: i) adding an acid to the demulsified suspension to adjust it to a pH of 5.5 to 8.5; ii) subsequently separating the resulting oil-containing light phase from the water, salt and cell debris-containing heavy phase; wherein: after lysing cells in step b), and prior to steps c) and d), the suspension is concentrated to a total dry matter content of 30 to 60 wt.-% by evaporation of water; more than 90 wt.-% of the oil contained in the initial biomass is separated and isolated; the method is carried out without the addition of any salts for salting out the oil. 2. The method of claim 1 , wherein, in step c) the suspension of lysed cells obtained in step b) is heated to a temperature of 85° C. to 95° C., and the pH is adjusted to a value of 9.0 to 11.0 and in step d), the temperature and pH are maintained for a period of 20 to 36 hours. 3. The method of claim 1 , comprising as a further step the conversion of the water, salt, residual oil and cell debris containing heavy phase into a dried biomass with a total dry matter content of more than 90 wt.-%. 4. The method of claim 3 , wherein conversion into a dried biomass is carried out by concentrating the heavy phase to a dry matter content of 30-50 wt.-% and subsequently spray granulating using a fluidized bed granulator. 5. The method of claim 1 , wherein the suspension is provided as a fermentation broth with a biomass density of at least 80 g/l. 6. The method of claim 5 , wherein the cells are selected from algae, fungi, protists, bacteria, microalgae, plant cells, and mixtures thereof. 7. The method of claim 5 wherein the cells are of the genus Schizochytrium. 8. The method of claim 4 , wherein the suspension is provided as a fermentation broth with a biomass density of at least 80 g/l. 9. The method of claim 8 , wherein the cells are selected from algae, fungi, protists, bacteria, microalgae, plant cells, and mixtures thereof. 10. The method of claim 8 , wherein the cells are of the genus Schizochytrium. 11. The method of claim 1 , wherein separation of step e)ii) is by filtration or centrifugation. 12. The method of claim 1 , wherein, the suspension is concentrated to a total dry matter content of preferably 35 to 55 wt.-% by evaporation of water at a temperature not higher than 100° C. 13. The method of claim 12 , wherein said temperature is 80° C. to 90° C.
by melting out · CPC title
by fermentation of natural products, e.g. of vegetable material, animal waste material or biomass · CPC title
Fatty acids; Fats; Products containing oils or fats · CPC title
by enzymes or microorganisms, living or dead · CPC title
Fats; Fatty oils; Ester-type waxes; Higher fatty acids, i.e. having at least seven carbon atoms in an unbroken chain bound to a carboxyl group; Oxidised oils or fats · CPC title
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