Methods for treatment of edible oils
AssigneeKraft General Foods, Inc.
InventorsR. G. Krishnamurthy, Neil R. Widlak, Joel J. Wang
Life of this patent
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Abstract
Improved methods for treatment of edible oils such as soybean oil and cottonseed oil to improve its stability, flavor and/or to deodorize the oil.
Claims9
A method for deodorizing an edible oil selected from the group consisting of edible vegetable oils and edible animal fats and mixtures thereof comprising the steps of deoxygenating the oil to provide a deoxygenated oil, heating the deoxygenated oil to a temperature in the range of from about 325.degree. F. to about 550.degree. F., continuously conducting the heated deoxygenated oil through a nitrogen, contacting zone having a solid surface to volume ratio of at least about 30 square feet of surface area per cubic foot of nitrogen contacting zone volume and continuously introducing substantially oxygen-free nitrogen having less than one part by weight per million of oxygen in a countercurrent manner through the heated oil in the nitrogen contacting zone at about atmospheric pressure conditions for a time period of at least about 5 minutes at an oil to gas weight to weight ratio in the range of from about 1.2 to about 4.5, and cooling the oil which has been conducted through the nitrogen contacting zone under oxygen excluding conditions to provide a deodorized vegetable oil.
A method for deodorizing an edible oil selected from the group consisting of edible vegetable oils and edible animal fats and mixtures thereof comprising the steps of deoxygenating the oil to provide a deoxygenated oil, blending the oil with a hydrogenation catalyst, heating the deoxygenated oil to a temperature in the range of from about 100.degree. F. to about 375.degree. F., contacting the oil and catalyst blend with hydrogen to subject the oil to hydrogen reducing conditions at a partial pressure of hydrogen of about 1 atmosphere or less without substantially reducing the unsaturated fatty triglycerides contact of the oil such that the hydrogen reduction condition is 1.3 or less, continuously conducting the heated deoxygenated oil through a nitrogen contacting zone having a solid surface to volume ratio of at least about 30 square feet of surface area per cubic foot of nitrogen contacting zone volume and continuously introducing substantially oxygen-free nitrogen having less than one part by weight per million of oxygen in a countercurrent manner through the heated oil in the nitrogen contacting zone that is not under vacuum, for a time period of at least about 5 minutes, at an oil to gas weight to weight ratio in the range of from about 1.2 to about 4.5, and cooling the oil which has been conducted through the nitrogen contacting zone under oxygen excluding conditions to provide a deodorized vegetable oil.
Dependencies are inferred from the claim text.