Patent US3960702A successfully refreshed from Google Patents.
US3960702A
Expired / Lapsed
US
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Vapor phase water process for retorting oil shale
Assignee: Marathon Oil Co
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Filing: 1974-08-08
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Granted: 1976-06-01
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Expires: 1994-08-08
Abstract
Abstract Oil shale is retorted using vapor phase water at about 850°-950°F, at a superficial gas velocity of about 20 feet per minute and at a pressure in the range of from about 1 to about 150 p.s.i.a.
Inventors
- 👤 Victor D. Allred
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 17:33
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/02; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
106 words
In a process for the recovery of organic values from oil shale by contacting said oil shale with superheated water vapor, the improvement comprising enhancing the recovery of said hydrocarbon values by, in combination, a. contacting particles of said oil shale with said superheated water vapor at a surperficial gas velocity of at least 20 feet per minute and at a pressure in the range of from about 1 to about 150 p.s.i.a., b. providing said contact with said superheated water vapor at a temperature of from about 850° to 950°F., to produce an effluent stream comprising superheated water vapor, hydrocarbon vapors, hydrogen, and carbon oxides.
Claim 2
Dependent Claim
106 words
In a process for the recovery of organic values from oil shale by contacting said oil shale with superheated water vapor, the improvement comprising enhancing the recovery of said hydrocarbon values by, in combination, a. contacting particles of said oil shale with said superheated water vapor at a surperficial gas velocity of at least 20 feet per minute and at a pressure in the range of from about 1 to about 150 p.s.i.a., b. providing said contact with said superheated water vapor at a temperature of from about 850° to 950°F., to produce an effluent stream comprising superheated water vapor, hydrocarbon vapors, hydrogen, and carbon oxides.
Claim 3
Dependent Claim
80 words
A process according to claim 1 additionally comprising the steps of: c. treating said effluent stream to condense at least a portion of said superheated water vapor and said hydrocarbons to form an immiscible stream comprising water and oil, and gases (comprising hydrogen) d. physically separating said oil and said water and said gases, and e. recycling at least a portion of said water by vaporizing it to form surperheated water vapor for contact with additional quantities of oil shale.
Claim 4
Dependent Claim
24 words
A process according to claim 1 wherein said superficial velocity is in the range of from about 20 to about 1000 feet per minute.
Claim 5
Dependent Claim
23 words
A process according to claim 1 wherein said temperature during said contact is in the range of from about 850° to about 880°F.
Claim 6
Dependent Claim
28 words
A process according to claim 2 wherein at least a portion of said hydrogen is utilized to hydrotreat said hydrocarbons to reduce the sulfur and nitrogen contents thereof.
Claim 7
Dependent Claim
17 words
A process according to claim 1 wherein the pressure is from about 2 to about 100 psia.
References Cited (Backward Citations)
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-06-01 | 1979-12-01 | 1980-06-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-06-01 | 1983-12-01 | 1984-06-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-06-01 | 1987-12-01 | 1988-06-01 | $7700.00 | Window Closed / Lapsed |