Use of marine algae for co-producing alkenones, alkenone derivatives, and co-products
US-10208321-B2 · Feb 19, 2019 · US
US11634738B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11634738-B2 |
| Application number | US-202117388298-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 29, 2021 |
| Priority date | Dec 17, 2009 |
| Publication date | Apr 25, 2023 |
| Grant date | Apr 25, 2023 |
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A method comprising a series of selective extraction techniques for the parallel production of biodiesel and isolation of several valuable co-products including an alkenone hydrocarbon mixture of the kerosene/jet fuel range (primarily C10-, C12-, and C17-hydrocarbons) and fucoxanthin, a high-valued carotenoid, from the marine alkenone-producing microalgae Isochrysis.
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The invention claimed is: 1. A method of isolating at least one product from algae, the method comprising: (a) growing an algal mariculture capable of producing alkenones; (b) extracting the algal mariculture with a non-polar liquid solvent to produce an extraction mixture; (c) separating the extraction mixture into at least a first fraction and a second fraction, wherein the first fraction is a lipid-containing mixture including alkenones and less than 50% (w/v) fatty acid methyl esters (FAMEs); and (d) isolating a mixture of alkenones, lipids, and FAMEs from the first fraction. 2. The method of claim 1 , further comprising the step of isolating alkenones from said mixture of alkenones, lipids, and FAMEs. 3. The method of claim 1 , wherein the algal mariculture comprises an algal family selected from one or more of the Isochrysis family, the Emiliania family, and the Gephyrocapsa family. 4. The method of claim 1 , wherein the non-polar solvent contains no fatty acids or fatty acid derivatives. 5. The method of claim 1 , wherein the algal mariculture contains at least 5% alkenones (w/w) relative to the starting dry weight of the algal mariculture. 6. The method of claim 1 , further comprising the step of dehydrating the algal mariculture. 7. The method of claim 6 , wherein the dehydration is performed by one or more methods consisting of lyophilization, evaporation with or without the addition of solvents, vacuum drying, drum drying, hot air exposure, dielectric drying, supercritical drying, and natural air drying, or a combination thereof. 8. The method of claim 1 , further comprising the step of isolating alkenones from the first fraction by combining the first fraction with a polar solvent or a partially polar solvent selected from one or more of chloromethane, dichloromethane, dichloroethane, tetrahydrofuran, dimethylformamide, acetonitrile, nitromethane, propylene, carbonate, formic acid, butanol, isopropanol, methyltetrahydrofuran, trifluoromethylbenzene, ethyl acetate, ethyl ether, acetone, dimethyl sulfoxide, alcohols, acetic acid, esters, or ethers. 9. The method of claim 8 , wherein the separation with the polar solvent or partially polar solvent produces a third fraction comprising neutral lipids. 10. The method of claim 1 , further comprising the step of isolating a mixture of alkenones and lipids from said mixture of alkenones, lipids, and FAMEs. 11. The method of claim 2 , wherein the isolated alkenones are recrystallized in a second solvent. 12. The method of claim 1 , further comprising the step of isolating a co-product from the second fraction. 13. The method of claim 12 , wherein said co-product from second fraction is a carotenoid. 14. The method of claim 12 , wherein said co-product from second fraction is a pigment. 15. The method of claim 14 , wherein said co-product from second fraction is fucoxanthin. 16. The method of claim 1 , further comprising the step of isolating a co-product from the first fraction. 17. The method of claim 16 , wherein said co-product is an acylglycerol.
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