Method for suppressing coloration of frying fats and oils composition
US-11118132-B2 · Sep 14, 2021 · US
US9765280B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9765280-B2 |
| Application number | US-201515120942-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 13, 2015 |
| Priority date | Mar 14, 2014 |
| Publication date | Sep 19, 2017 |
| Grant date | Sep 19, 2017 |
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A method for producing a blown and stripped biorenewable oil is provided. The method may include the steps of (a) heating a biorenewable oil to at least 90° C.; (b) exposing an oxygen containing stream to the heated oil to produce a blown oil having a viscosity of at least 40 cSt at 40° C.; (c) adding a base metal catalyst to the blown oil; and (d) stripping the blown oil from step (c) until the stripped oil has an acid value of from about 1 mg KOH/g to about 20 mg KOH/g; wherein the stripped oil from step (d) has a flash point of at least 220° C.
Opening claim text (preview).
We claim: 1. A method for producing a blown and stripped biorenewable oil, the method comprising the steps of: (a) heating a composition comprising biorenewable oil and a first catalyst to at least 90° C.; (b) exposing an oxygen containing stream to the heated composition from step (a) to produce a blown oil having a viscosity of at least 40 cSt at 40° C.; and (c) stripping the blown oil, in the presence of a second catalyst, to produce a stripped oil having an acid value of from about 1 mg KOH/g to about 20 mg KOH/g; wherein the first catalyst and the second catalyst are different. 2. The method of claim 1 , wherein the composition in step (a) is heated to about 115° C. 3. The method of claim 1 , wherein the oxygen containing stream is an oxygen enriched stream derived from air. 4. The method of claim 1 , wherein the oxygen containing stream comprises hydrogen peroxide. 5. The method of claim 1 , wherein the stripping step includes bodying reactions. 6. The method of claim 1 , wherein the first catalyst is a base metal catalyst comprising a transition metal. 7. The method of claim 1 , wherein step (a) includes adding the first catalyst in an amount ranging from about 200 ppm to about 1000 ppm. 8. The method of claim 1 , wherein the composition in step (a) further comprises a peroxide initiator. 9. The method of claim 1 , wherein the composition in step (a) further comprises tung oil. 10. The method of claim 1 , wherein the second catalyst comprises potassium hydroxide. 11. The method of claim 1 , wherein the second catalyst is a base metal catalyst. 12. The method of claim 11 , wherein the base metal catalyst comprises metal selected from the group consisting of potassium, calcium, sodium, magnesium, and combinations thereof. 13. The method of claim 1 , wherein the second catalyst is present in an amount ranging from about 250 ppm to about 1200 ppm. 14. The method of claim 1 , further including the step of adding a polyol to the stripped oil before, during, or after step (c). 15. The method of claim 14 , wherein the polyol comprises glycerol. 16. The method of claim 1 , wherein the viscosity of the stripped oil produced in step (c) ranges from about 45 cSt to about 70 cSt at 40° C. 17. The method of claim 1 , wherein the stripped oil produced in step (c) comprises: (a) from about 2% to about 10% by weight free fatty acids; (b) from about 12% to about 22% by weight diacylgycerides; (c) from about 50% to about 70% by weight triglycerides; and (d) from about 5% to about 20% by weight dimers and trimers content, collectively. 18. The method of claim 1 , wherein the stripped oil produced in step (c) has a flash point of at least 220° C. 19. The method of claim 1 , wherein the stripped oil produced in step (c) has a hydroxyl value of 10 to 70. 20. The method of claim 1 , wherein the stripped oil produced in step (c) has an acid value of from about 1 mg KOH/g to about 20 mg KOH/g.
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