Production of dihydrosterculic acid and derivatives thereof
US-2016348123-A1 · Dec 1, 2016 · US
US12349693B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12349693-B2 |
| Application number | US-201816196040-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 20, 2018 |
| Priority date | Feb 10, 2011 |
| Publication date | Jul 8, 2025 |
| Grant date | Jul 8, 2025 |
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A refined oil composition having a reduced 3-MCPD ester and/or glycidyl ester content and methods of preparation thereof.
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The invention claimed is: 1. A process for the production of a refined oil having a reduced 3-MCPD ester and glycidyl ester content, the process comprising: subjecting an oil to bleaching and deodorization consisting of: (a) bleaching the oil with activated bleaching clay to form a first bleached oil, (b) deodorizing the first bleached oil at a temperature in a range of 200° C. to 280° C. to form a first deodorized oil, (c) bleaching the first deodorized oil with activated bleaching clay to form a second bleached oil, and (d) deodorizing the second bleached oil at a temperature of 130° C. to 160° C.; wherein: the bleaching and deodorization reduce the combined 3-MCPD ester and glycidyl ester content of the refined oil to no more than 5 ppm and reduce free fatty acid (FFA) content of the refined oil to less than 0.1% by weight; and the oil is palm oil containing 3-MCPD ester and glycidyl ester. 2. The process according to claim 1 wherein the bleaching (c) is carried out at a temperature below 80° C. 3. The process according to claim 1 further comprising one or more alkali treatment steps. 4. The process according to claim 1 , wherein the combined 3-MCPD ester and glycidyl ester content is no more than 3 ppm. 5. The process according to claim 1 , wherein the combined 3-MCPD ester and glycidyl ester content is no more than 2 ppm. 6. The process according to claim 1 further comprising a degumming step prior to subjecting the oil to bleaching and deodorization steps. 7. The process according to claim 1 further comprising one or more of the following additional steps selected from neutralization, dewaxing, fractionation, hydrogenation, interesterification, blending with two or more different refined oils, or combinations thereof. 8. The process according to claim 1 , wherein the refined oil has a combined 3-MCPD ester and glycidyl ester content that is at least 50% lower than that of an oil obtained by standard physical refining, wherein standard physical refining comprises degumming, bleaching, and deodorization. 9. The process according to claim 1 , wherein the refined oil has a combined 3-MCPD ester and glycidyl ester content that is at least 90% lower than that of an oil obtained by standard physical refining, wherein standard physical refining comprises degumming, bleaching, and deodorization. 10. The process according to claim 1 , wherein the combined 3-MCPD ester and glycidyl ester content of the refined oil is no more than 1 ppm. 11. The process according to claim 1 , wherein the combined 3-MCPD ester and glycidyl ester content of the refined oil is from 0.3 ppm to 1 ppm.
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