US3943155A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Simultaneous refining and dewaxing of crude vegetable oil
Assignee: Procter and Gamble Co
•
Filing: 1974-05-13
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Granted: 1976-03-09
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Expires: 1994-05-13
Abstract
Abstract A process for refining and dewaxing crude vegetable oils using only one separation step which removes both the hydrophilic and waxy components from the crude oil. An alkali refining/dewaxing treatment is employed on crude oil at a temperature of from about 15°F to about 45°F.
Inventors
- 👤 Herbert Thomas Young
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-27 14:01
CPC Classifications
C; C11; C11B; C11B3/00; C11B3/02; C11B3/06; C11B3/001
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
151 words
A process for simultaneously removing the hydrophilic and waxy components from crude vegetable oil comprising the steps of: a. gently agitating a crude vegetable oil at a temperature of from about 15°F to about 45°F; b. contacting the agitated crude vegetable oil with at least one equivalent of aqueous alkali per mole of free fatty acid present in the crude vegetable oil while maintaining the temperature of the mixture of vegetable oil and aqueous alkali in the range of from about 15°F to about 45°F, thereby to form an emulsion of hydrophilic and waxy components; c. mixing a phosphoric acid solution in an amount of from about 0.05 to about 0.2 percent by weight of said crude vegetable oil with said mixture of vegetable oil and aqueous alkali, thereby to break said emulsion into a two-phase system; and d. separating the oil phase from the aqueous phase of said two-phase system.
Claim 2
Dependent Claim
151 words
A process for simultaneously removing the hydrophilic and waxy components from crude vegetable oil comprising the steps of: a. gently agitating a crude vegetable oil at a temperature of from about 15°F to about 45°F; b. contacting the agitated crude vegetable oil with at least one equivalent of aqueous alkali per mole of free fatty acid present in the crude vegetable oil while maintaining the temperature of the mixture of vegetable oil and aqueous alkali in the range of from about 15°F to about 45°F, thereby to form an emulsion of hydrophilic and waxy components; c. mixing a phosphoric acid solution in an amount of from about 0.05 to about 0.2 percent by weight of said crude vegetable oil with said mixture of vegetable oil and aqueous alkali, thereby to break said emulsion into a two-phase system; and d. separating the oil phase from the aqueous phase of said two-phase system.
Claim 3
Dependent Claim
22 words
The process of claim 1 wherein said crude vegetable oil is reduced to a temperature of from about 20°F to about 30°F.
Claim 4
Dependent Claim
13 words
The process of claim 1 wherein the aqueous alkali solution is sodium hydroxide.
Claim 5
Dependent Claim
28 words
The process of claim 3 wherein the aqueous alkali solution has a concentration in water of from about 1.0 to about 3.0 percent by weight of sodium hydroxide.
Claim 6
Dependent Claim
25 words
The process of claim 1 wherein the aqueous alkali solution comprises of from about 15 to about 50 percent by weight of the vegetable oil.
Claim 7
Dependent Claim
25 words
The process of claim 5 wherein the aqueous alkali solution comprises of from about 20 to about 40 percent by weight of the vegetable oil.
Claim 8
Dependent Claim
44 words
The process of claim 1 wherein sufficient aqueous alkali solution is added to the crude vegetable oil such that there is from about 3 alkali equivalents to about 5 alkali equivalents for each mole of free fatty acid present in said crude vegetable oil.
Claim 9
Dependent Claim
28 words
The process of claim 1 wherein the phosphoric acid solution is in a concentration of from about 20 to about 100 percent by weight of the absolute acid.
Claim 10
Dependent Claim
27 words
The process of claim 1 wherein the phosphoric acid solution is in a concentration of from about 20 to about 40 percent by weight of absolute acid.
Claim 11
Dependent Claim
30 words
The process of claim 1 wherein said phosphoric acid solution is added in an amount of from about 0.05 to about 0.15 percent by weight of the crude vegetable oil.
Claim 12
Dependent Claim
26 words
The process of claim 1 wherein said phosphoric acid solution is added in an amount of about 0.10 percent by weight of the crude vegetable oil.
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) | 1979-03-09 | 1979-09-08 | 1980-03-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-03-09 | 1983-09-08 | 1984-03-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-03-09 | 1987-09-08 | 1988-03-09 | $7700.00 | Window Closed / Lapsed |