초록 ▼

The invention is generally directed to conjugated linoleic acid (CLA)-rich vegetable oil production from linoleic rich oils by heterogeneous catalysis. A heterogeneous catalytic vacuum distillation process is used under high temperature conditions to isomerize linoleic acid in triacylglyceride veget

The invention is generally directed to conjugated linoleic acid (CLA)-rich vegetable oil production from linoleic rich oils by heterogeneous catalysis. A heterogeneous catalytic vacuum distillation process is used under high temperature conditions to isomerize linoleic acid in triacylglyceride vegetable oils to CLA to produce CLA-rich oils. After processing, the catalyst may be removed by filtration or centrifugation to obtain high quality, CLA-rich oils. The CLA-rich oils may then serve as a potent and bioactive nutraceutical and can be incorporated into various food products, such as a CLA-rich dressing, margarine or chips.

대표청구항 ▼

1. A process for producing conjugated linoleic acid-rich oil, said process comprising the steps of: a. mixing a linoleic acid-rich oil with a catalytic amount of ruthenium, rhodium, silver, or nickel on a carbon or silica support to form an oil-catalyst mixture; andb. heterogeneous catalysis via vac

1. A process for producing conjugated linoleic acid-rich oil, said process comprising the steps of: a. mixing a linoleic acid-rich oil with a catalytic amount of ruthenium, rhodium, silver, or nickel on a carbon or silica support to form an oil-catalyst mixture; andb. heterogeneous catalysis via vacuum steam distillation of said oil-catalyst mixture at a pressure between approximately 1 mm Hg and approximately 2 mm Hg, at a temperature between 221° C. and approximately 282° C., and for up to approximately 192 minutes to produce said conjugated linoleic acid-rich oil. 2. The process of claim 1 further comprising the step of extracting said metal from said conjugated linoleic acid-rich oil. 3. The process of claim 2 further comprising the step of extracting said metal from said conjugated linoleic acid-rich oil via filtration or centrifugation. 4. The process of claim 1 wherein said linoleic acid-rich oil is a triacylglyceride vegetable oil. 5. The process of claim 4 wherein said triacylglyceride vegetable oil is selected from the group consisting of soy, sunflower, corn, cottonseed or peanut oil. 6. The process of claim 1 wherein said catalysis step further comprises heterogeneous catalysis via vacuum steam distillation of said oil-catalyst mixture for between approximately 108 minutes and approximately 192 minutes to produce said conjugated linoleic acid-rich oil. 7. The process of claim 1 wherein said catalysis step further comprises heterogeneous catalysis via vacuum steam distillation of said oil-catalyst mixture for between approximately 60 minutes and approximately 180 minutes to produce said conjugated linoleic acid-rich oil. 8. The process of claim 1 wherein said temperature conditions are between greater than 221° C. and approximately 240° C. 9. The process of claim 1 wherein said catalysis step further comprises heterogeneous catalysis via vacuum steam distillation of said oil-catalyst mixture in a continuous flow bath. 10. The process of claim 1 wherein said catalysis step further comprises a two-phase heterogeneous catalysis via vacuum steam distillation of said oil-catalyst mixture. 11. The process of claim 1 wherein said catalytic amount of said ruthenium, rhodium, silver, or nickel comprises between approximately 0.64% and approximately 1% of said ruthenium, rhodium, silver, or nickel. 12. The process of claim 1 wherein said catalytic amount of said ruthenium, rhodium, silver, or nickel comprises between 0.21% to approximately 1% of said ruthenium, rhodium, silver, or nickel. 13. The process of claim 12 wherein said catalytic amount of said ruthenium, rhodium, silver, or nickel is approximately 0.64% of a ruthenium catalyst or approximately 1% of a nickel catalyst. 14. A process for enriching a linoleic acid-rich vegetable oil, said process comprising the step of vacuum steam distilling said linoleic acid-rich vegetable oil in the presence of a transition metal catalyst, in the absence of a solvent or iodine, at a temperature between 221° C. and approximately 282° C., at a pressure between approximately 1 mm Hg and approximately 2 mm Hg, and for up to approximately 192 minutes to produce a conjugated linoleic acid-rich oil; and wherein said transition metal catalyst is between 0.21% to approximately 1% of a ruthenium, rhodium, silver, or nickel catalyst. 15. The process of claim 14 further comprising the step of extracting said metal catalyst from said conjugated linoleic acid-rich oil. 16. The process of claim 15 further comprising the step of extracting said metal catalyst from said conjugated linoleic acid-rich oil via filtration or centrifugation. 17. The process of claim 14 wherein said linoleic acid-rich oil is a triacylglyceride vegetable oil. 18. The process of claim 17 wherein said triacylglyceride vegetable oil is selected from the group consisting of soy, sunflower, corn, cottonseed or peanut oil. 19. The process of claim 14 wherein said step of steam distilling further comprises vacuum steam distilling said linoleic acid-rich vegetable oil approximately 60 minutes to approximately 192 minutes to produce said conjugated linoleic acid-rich oil. 20. The process of claim 19 wherein said step of steam distilling further comprises vacuum steam distilling said linoleic acid-rich vegetable oil for between approximately 108 minutes and approximately 180 minutes to produce said conjugated linoleic acid-rich oil. 21. The process of claim 14 wherein said temperature is between greater than 221° C. and approximately 240° C. 22. The process of claim 14 wherein said steam distilling step further comprises vacuum steam distilling said linoleic acid-rich vegetable oil in a continuous flow bath. 23. The process of claim 22 wherein said steam distilling step further comprises vacuum steam distilling said linoleic acid-rich vegetable oil at said temperature between greater than 221° C. and approximately 240° C. for between approximately 108 minutes and approximately 180 minutes to produce said conjugated linoleic acid-rich oil. 24. The process of claim 14 wherein said transition metal catalyst comprises between 0.32% to approximately 0.75% of ruthenium catalyst on a carbon support. 25. The process of claim 14 wherein said transition metal catalyst is approximately 0.64% of a ruthenium catalyst or approximately 1% of a nickel catalyst on a carbon support.