Patent US4035402A successfully refreshed from Google Patents.
US4035402A
Expired / Lapsed
US
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Dewaxing process for vegetable oils
Assignee: Procter and Gamble Co
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Filing: 1975-09-30
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Granted: 1977-07-12
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Expires: 1995-09-30
Abstract
Abstract This invention relates to an improved process for dewaxing vegetable oils containing free fatty acid impurities, wax and other insoluble matter, which comprises: chilling a refined and water-washed or filtered vegetable oil, mixing the chilled vegetable oil with a dilute alkaline solution; gently agitating the resulting mixture, centrifuging the mixture and separating a heavy phase which contains wax and other impurities from a light phase which may then be bleached and deodorized to form a clear oil. The invention further relates to a reliable process for producing salad oils and other clear oils which remain clear at ambient to refrigerator temperatures.
Inventors
- 👤 Leon Levine
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 19:34
CPC Classifications
C; C11; C11B; C11B3/00; C11B3/02; C11B3/06
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
119 words
A process for dewaxing vegetable oils comprising the steps of: (a) providing a vegetable oil pre-refined until analysis of said oil shows less than 0.1% soap and less than 0.1% free fatty acid content, said oil being chilled to a temperature of less than about 60° F.; (b) holding said refined oil at said temperature for longer than one hour; (c) mixing said refined vegetable oil of step (b) with an aqueous alkaline solution; (d) agitating in a low shear-high circulation manner the mixture of step (c) for at least 1/2 hour, to uniformly disperse the alkaline solution without forming an inseparable emulsion; and (e) separating the agitated mixture to provide a wax-containing water phase and a dewaxed oil.
Claim 2
Dependent Claim
119 words
A process for dewaxing vegetable oils comprising the steps of: (a) providing a vegetable oil pre-refined until analysis of said oil shows less than 0.1% soap and less than 0.1% free fatty acid content, said oil being chilled to a temperature of less than about 60° F.; (b) holding said refined oil at said temperature for longer than one hour; (c) mixing said refined vegetable oil of step (b) with an aqueous alkaline solution; (d) agitating in a low shear-high circulation manner the mixture of step (c) for at least 1/2 hour, to uniformly disperse the alkaline solution without forming an inseparable emulsion; and (e) separating the agitated mixture to provide a wax-containing water phase and a dewaxed oil.
Claim 3
Dependent Claim
17 words
The process of claim 1 wherein the vegetable oil of step (a) contains less than 0.05% soap.
Claim 4
Dependent Claim
20 words
The process of claim 1 wherein the vegetable oil of step (a) contains less than 0.05% free fatty acid content.
Claim 5
Dependent Claim
21 words
The process of claim 1 wherein the oil temperature of step (a) is from about 30° F. to about 50° F.
Claim 6
Dependent Claim
15 words
The process of claim 1 wherein the oil temperature of step (a) is 40° F.
Claim 7
Dependent Claim
30 words
The process of claim 1 wherein the aqueous alkaline solution of step (c) comprises from about 10% to about 30% of the combined weight of vegetable oil and alkaline solution.
Claim 8
Dependent Claim
30 words
The process of claim 6 wherein the aqueous alkaline solution is sodium hydroxide in a concentration of from about 1% to about 2.5% by weight of sodium hydroxide in water.
Claim 9
Dependent Claim
23 words
The process of claim 1 wherein the agitation in step (c) is provided by two 6-inch marine impellers operated at about 100 rpm.
Claim 10
Dependent Claim
10 words
The process of claim 1 wherein the process is continuous.
Claim 11
Dependent Claim
13 words
The process of claim 1 wherein the process is conducted in batch fashion.
Claim 12
Dependent Claim
18 words
The process of claim 1 wherein the aqueous alkaline solution is a solution of a fatty acid soap.
Claim 13
Dependent Claim
25 words
The process of claim 1 wherein the aqueous alkaline solution is a solution of an alkali metal soap of from 8 to 22 carbon atoms.
Claim 14
Dependent Claim
18 words
The process of claim 12 wherein the aqueous alkaline solution is a solution of an alkali metal oleate.
Claim 15
Dependent Claim
230 words
A process for dewaxing vegetable oils previously refined and which contain waxes which precipitate at refrigerator temperatures comprising the steps of: (a) providing a vegetable oil pre-refined until analysis of said oil showed less than 0.05% soap and from about 0.01% to less than about 0.05% free fatty acid content, said oil being chilled to a temperature of about 30° F. to about 50° E., (b) holding said refined oil at said temperature for longer than 1 hour; (c) diluting said refined vegetable oil of step (b) by admixing with from about 10% to 30% by weight of an aqueous alkali solution of about 1.5% by weight concentration of an alkali selected from the group consisting of sodium hydroxide, sodium bicarbonate, potassium hydroxide, calcium hydroxide, magnesium hydroxide and ammonia, (d) agitating in a low shear-high circulation manner the mixture of step (c) for at least 1/2 hour, to uniformly disperse the alkali solution without forming an inseparable emulsion; and (e) then centrifuging the agitated mixture to separate the wax-containing water phase and to provide a dewaxed oil in which the soap content is less than 0.03% by weight, water is less than 0.3%, and which oil after conventional blending and deodorization is suitable for use as a salad oil and has excellent refrigerator clarity of greater than 100 hours at 32° F. and longer than two weeks at 40° F.
Claim 16
Dependent Claim
230 words
A process for dewaxing vegetable oils previously refined and which contain waxes which precipitate at refrigerator temperatures comprising the steps of: (a) providing a vegetable oil pre-refined until analysis of said oil showed less than 0.05% soap and from about 0.01% to less than about 0.05% free fatty acid content, said oil being chilled to a temperature of about 30° F. to about 50° E., (b) holding said refined oil at said temperature for longer than 1 hour; (c) diluting said refined vegetable oil of step (b) by admixing with from about 10% to 30% by weight of an aqueous alkali solution of about 1.5% by weight concentration of an alkali selected from the group consisting of sodium hydroxide, sodium bicarbonate, potassium hydroxide, calcium hydroxide, magnesium hydroxide and ammonia, (d) agitating in a low shear-high circulation manner the mixture of step (c) for at least 1/2 hour, to uniformly disperse the alkali solution without forming an inseparable emulsion; and (e) then centrifuging the agitated mixture to separate the wax-containing water phase and to provide a dewaxed oil in which the soap content is less than 0.03% by weight, water is less than 0.3%, and which oil after conventional blending and deodorization is suitable for use as a salad oil and has excellent refrigerator clarity of greater than 100 hours at 32° F. and longer than two weeks at 40° F.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-07-11 | 1981-01-10 | 1981-07-12 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-07-11 | 1985-01-10 | 1985-07-12 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-07-11 | 1989-01-10 | 1989-07-12 | $7700.00 | Window Closed / Lapsed |