Oil Crystallization Promoter, Preparation Method Therefor and Use Thereof
US-2024407384-A1 · Dec 12, 2024 · US
US2016338374A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016338374-A1 |
| Application number | US-201515110716-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 8, 2015 |
| Priority date | Jan 8, 2014 |
| Publication date | Nov 24, 2016 |
| Grant date | — |
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The present invention relates to a sesame oil and a method for preparing the same. The present invention provides a sesame oil having high lignan and tocopherol contents by preparing the sesame oil using an extraction and fractionation technique using a supercritical fluid, and a method for preparing the same. Also, the present invention provides a sesame oil having high lignan and tocopherol contents and a low free fatty acid content by preparing the sesame oil using an extraction and fractionation technique using a supercritical fluid and deacidifying the sesame oil, and a method for preparing the same.
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1 . Sesame oil having a lignan content of 7,800 ppm or more and a tocopherol content of 300 ppm to 700 ppm. 2 . The sesame oil according to claim 1 , wherein the sesame oil has an acid value of 4.0 or less. 3 . The sesame oil according to claim 1 , wherein the lignan comprises at least one selected from sesamin, episesamin, sesamolin, sesamol, sesamolinol, sesaminol, and episesaminol. 4 . The sesame oil according to claim 1 , wherein the tocopherol is γ-tocopherol. 5 . A method of preparing sesame oil, comprising: extracting sesame seeds using a supercritical fluid to provide sesame extract; and separating the supercritical fluid from a mixture of the supercritical fluid and the sesame extract, wherein extraction of the sesame extract is performed at an S/F ratio of more than 0, and 30 or less. 6 . A method of preparing sesame oil, comprising: extracting sesame seeds using a supercritical fluid to provide sesame extract; separating the supercritical fluid from a mixture of the supercritical fluid and the sesame extract; and removing free fatty acids by adding at least one free fatty acid removal agent selected from among magnesium silicate, magnesium oxide, and sodium hydroxide to the obtained sesame extract. 7 . (canceled) 8 . The method according to claim 6 , wherein extraction of the sesame extract is performed at an S/F ratio of more than 0, and 30 or less. 9 . The method according to claim 5 , wherein extraction of the sesame extract is performed at a pressure of 120 bar to 700 bar and at a temperature of 40° C. to 90° C. 10 . The method according to claim 5 , wherein separation of the supercritical fluid is performed at a pressure of 40 bar to 70 bar and at a temperature of 20° C. to 50° C. 11 . The method according to claim 5 , wherein the supercritical fluid is carbon dioxide. 12 . (canceled) 13 . The method according to claim 5 , further comprising: obtaining a first sesame oil by primary fractionation of the separated sesame extract at an S/F ratio of more than 0, and 10 or less; and obtaining a second sesame oil by secondary fractionation of the separated sesame extract at an S/F ratio of more than 10, and 30 or less. 14 . The method according to claim 6 , comprising: obtaining a first sesame oil by primary fractionation of the separated sesame extract at an S/F ratio of more than 0, and 10 or less and obtaining a second sesame oil by secondary fractionation of the separated sesame extract at an S/F ratio of more than 10, and 30 or less before removal of free fatty acids; and removing free fatty acids from the first sesame oil. 15 . The method according to claim 6 , wherein magnesium silicate or magnesium oxide is added in an amount of 0.5 wt % to 4.0 wt % based on the weight of the sesame oil or the sesame extract. 16 . The method according to claim 6 , wherein sodium hydroxide is added in an amount of 0.1 wt % to 0.4 wt % based on the weight of the sesame oil or the sesame extract. 17 . The method according to claim 13 , wherein the first sesame oil, has a lignan content of 15,000 ppm or more and a tocopherol content of 300 ppm to 700 ppm. 18 . The method according to 17 , having free fatty acids in an amount of 1.0 wt % to 3.0 wt %. 19 . The method according to claim 13 , wherein the second sesame oil has a lignan content of 3,000 ppm or less and has an acid value of 0 to 1.0. 20 . (canceled) 21 . (canceled) 22 . The method according to claim 6 , wherein extraction of the sesame extract is performed at a pressure of 120 bar to 700 bar and at a temperature of 40° C. to 90° C. 23 . The method according to claim 6 , wherein separation of the supercritical fluid is performed at a pressure of 40 bar to 70 bar and at a temperature of 20° C. to 50° C. 24 . The method according to claim 6 , wherein the supercritical fluid is carbon dioxide.
Other edible oils or fats, e.g. shortenings or cooking oils (preservation of other edible oils A23B20/30) · CPC title
by extraction · CPC title
Food compositions, function of food ingredients or processes for food or foodstuffs · CPC title
Working-up · CPC title
Treatment with inorganic compounds (A23L5/273 takes precedence) · CPC title
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