Patent US4069141A successfully refreshed from Google Patents.
US4069141A
Expired / Lapsed
US
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Process for recovering fuel oil from topped crude
Assignee: Texaco Inc
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Filing: 1976-12-27
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Granted: 1978-01-17
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Expires: 1996-12-27
Abstract
Abstract A topped crude oil is admixed with a hydrocarbon solvent and centrifuged in the presence of a brine carrier to produce a hydrocarbon solvent-fuel oil mixture and a brine-asphalt-fuel oil mixture, the latter mixture being recovered and admixed with a ketone solvent which effects emulsion breaking and extracts residual fuel oil, a ketone solvent rich phase being subsequently recovered and subjected to fractionation to separate the fuel oil from the ketone solvent, the latter being recycled for further usage.
Inventors
- 👤 Thomas A. Lionetti
- 👤 Kenneth D. Miller
- 👤 Levi C. Parker
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 15:47
CPC Classifications
C; C10; C10G; C10G21/00; C10G21/003
Claims Analysis
Total Claims: 19
Claim 1
Independent Claim
104 words
A process for recovering fuel oil from a topped crude oil comprising: a. admixing said topped crude oil with a hydrocarbon solvent; b. centrifuging said mixture of said topped crude oil and said hydrocarbon solvent in the presence of a brine carrier; c. recovering a brine-asphalt-fuel oil mixture from said centrifuging step; d. admixing said brine-asphalt-fuel oil mixture with a normally liquid ketone solvent selected from the class consisting of aliphatic and alicyclic ketones having at least four carbon atoms; e. recovering a ketone rich phase from the mixture produced in step (d); and f. recovering said fuel oil from said ketone rich phase.
Claim 2
Dependent Claim
104 words
A process for recovering fuel oil from a topped crude oil comprising: a. admixing said topped crude oil with a hydrocarbon solvent; b. centrifuging said mixture of said topped crude oil and said hydrocarbon solvent in the presence of a brine carrier; c. recovering a brine-asphalt-fuel oil mixture from said centrifuging step; d. admixing said brine-asphalt-fuel oil mixture with a normally liquid ketone solvent selected from the class consisting of aliphatic and alicyclic ketones having at least four carbon atoms; e. recovering a ketone rich phase from the mixture produced in step (d); and f. recovering said fuel oil from said ketone rich phase.
Claim 3
Dependent Claim
27 words
The process of claim 1 wherein said hydrocarbon solvent is selected from the class consisting of aliphatic and alicyclic hydrocarbons having from seven to 15 carbon atoms.
Claim 4
Dependent Claim
20 words
The process of claim 1 wherein said hydrocarbon solvent comprises an aliphatic hydrocarbon having from seven to 15 carbon atoms.
Claim 5
Dependent Claim
13 words
The process of claim 3 wherein said hydrocarbon is primarily paraffinic in nature.
Claim 6
Dependent Claim
22 words
The process of claim 1 wherein the volume ratio of said hydrocarbon solvent to said topped crude oil is at least 2:1.
Claim 7
Dependent Claim
25 words
The process of claim 5 wherein said volume ratio of said hydrocarbon solvent to said topped crude oil is from about 2:1 to about 20:1.
Claim 8
Dependent Claim
21 words
The process of claim 1 wherein said centrifuging is conducted at a temperature of from about 30° to about 80° F.
Claim 9
Dependent Claim
31 words
The process of claim 1 wherein said brine-asphalt-fuel oil mixture is admixed with said ketone solvent in a volume ratio of ketone solvent to brine-asphalt-fuel oil mixture of greater than 0.5:1.
Claim 10
Dependent Claim
24 words
The process of claim 8 wherein said ratio of said ketone solvent to said brine-asphalt-fuel oil mixture is from about 0.5:1 to about 5:1.
Claim 11
Dependent Claim
20 words
The process of claim 1 wherein said ketone solvent comprises an aliphatic ketone having from four to 10 carbon atoms.
Claim 12
Dependent Claim
13 words
The process of claim 10 wherein said ketone solvent comprises methyl ethyl ketone.
Claim 13
Dependent Claim
22 words
The process of claim 11 wherein the volume ratio of said methyl ethyl ketone to said brine-asphalt-fuel oil mixture is about 1:1.
Claim 14
Dependent Claim
16 words
The process of claim 1 including recovering a fuel oil-hydrocarbon solvent mixture from said centrifuging step.
Claim 15
Dependent Claim
32 words
The process of claim 13 including treating said fuel oil-hydrocarbon solvent mixture to separate said hydrocarbon solvent from said fuel oil and recycling said hydrocarbon solvent for use in said centrifuging step.
Claim 16
Dependent Claim
33 words
The process of claim 14 including combining the fuel oil recovered in step (f) with the fuel oil separated from said fuel oil-hydrocarbon solvent mixture to provide a feed for a desulfurization process.
Claim 17
Dependent Claim
39 words
The process of claim 1 including recovering an asphalt rich phase from the mixture produced in step (d), admixing said asphalt rich phase with water to produce an aqueous asphalt mixture and recovering asphalt from said aqueous asphalt mixture.
Claim 18
Dependent Claim
33 words
The process of claim 1 including recovering a brine rich phase from the mixture produced in step (d) and recovering said brine from said brine rich phase for use in said centrifuging step.
Claim 19
Dependent Claim
21 words
The process of claim 17 including separating ketone solvent from said brine rich phase for admixture with said brine-asphalt-fuel oil mixture.
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) | 1981-01-16 | 1981-07-18 | 1982-01-17 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-01-16 | 1985-07-18 | 1986-01-17 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-01-16 | 1989-07-18 | 1990-01-17 | $7700.00 | Window Closed / Lapsed |