Blown and stripped blend of soybean oil and corn stillage oil
First Claim
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1. A method for producing a high viscosity, low volatiles blown stripped oil blend, the method comprising the steps of:
- (a) obtaining an oil blend;
(b) heating the oil blend to at least 90°
C.;
(c) passing air through the heated oil blend to produce a blown oil having a viscosity of at least 50 cSt at 40°
C.; and
(d) stripping the blown oil from step (c) to reduce an acid value of the blown oil to less than 5.0 mg KOH/gram;
wherein the oil resulting from step (d) has a hydroxyl number less than 40 mg KOH/gram.
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Abstract
A method for producing a high viscosity, low volatiles blown stripped oil blend is provided. The method may include the steps of: (i) obtaining an oil blend of corn stillage oil and soybean oil having a weight ratio of corn stillage oil to soybean oil of from about 1:2 to 3:1; (ii) heating the oil blend to at least 90° C.; (iii) passing air through the heated oil blend to produce a blown oil having a viscosity of at least 50 cSt at 40° C.; and (iv) stripping the blown oil from step (iii) to reduce an acid value of the blown oil to less than 5.0 mg KOH/gram.
77 Citations
26 Claims
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1. A method for producing a high viscosity, low volatiles blown stripped oil blend, the method comprising the steps of:
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(a) obtaining an oil blend; (b) heating the oil blend to at least 90°
C.;(c) passing air through the heated oil blend to produce a blown oil having a viscosity of at least 50 cSt at 40°
C.; and(d) stripping the blown oil from step (c) to reduce an acid value of the blown oil to less than 5.0 mg KOH/gram; wherein the oil resulting from step (d) has a hydroxyl number less than 40 mg KOH/gram. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 23, 24, 25)
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15. A method for producing a high viscosity, low volatiles blown, stripped oil blend, the method comprising the steps of:
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(a) obtaining an oil blend, the oil blend having an initial acid value of from 8 mg KOH/gram to 18 mg KOH/gram; (b) heating the oil blend to at least 90°
C.;(c) passing air through the heated oil blend to produce a blown oil blend; (d) stripping the blown oil blend to reduce the acid value of the blown oil blend to from 5 mg KOH/gram to 9 mg KOH/gram; (e) adding a sufficient amount of glycerin to the stripped blown oil from (d) to obtain a molar ratio of hydroxyl groups from the added glycerin to the free fatty acids present in the oil from (d) of from 1;
5 to less than 1;
1; and(f) stripping the oil from step (e) to a final acid value of about 3.5 mg KOH/gram or less. - View Dependent Claims (16, 17, 18, 19, 20, 21, 22, 26)
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Specification