US4197183A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Processing of tar sands
Assignee: Mobil Oil AS
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Filing: 1979-02-07
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Granted: 1980-04-08
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Expires: 1999-02-07
Abstract
Abstract Petroliferous material of tar sands is processed to recover both low and higher boiling distillate material in a sequential combination operation involving thermal distillation and solvent extraction. Residue of solvent extraction is gasified with hot sand product of gasification step used in the thermal distillation operation.
Inventors
- 👤 Costandi A. Audeh
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 07:31
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/002; C10G1/006
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
209 words
In a process for upgrading tar sands by the combination of thermal distillation to recover a distillate material boiling below about 850° F. and gasification of residue hydrocarbonaceous material remaining with the sand recovered from the thermal distillation operation to produce fuel gas and high temperature streams of sand particles, air and steam transferable for use in the process combination, the improvement which comprises effecting thermal distillation of tar sand admixed with hot sand particles obtained from said gasification step under conditions to obtain a hydrocarbon product of end boiling point within the range of 650° F. to about 1000° F., passing sand with residual oily higher boiling hydrocarbon material from said thermal distillation operation to a solvent extraction operation maintained under conditions to remove said higher boiling hydrocarbons other than asphaltic type organic material by solvent extraction, passing sand with asphaltic type organic material separated from solvent extracted material to said gasification zone maintained under conditions to produce a fuel gas product and hot sand particles, recovering solvent with extracted higher boiling hydrocarbons and separating to recover solvent from said higher boiling hydrocarbons, and using the hot fuel gas product and sand obtained from said gasification operation to provide heat to the above identified combination of processing steps.
Claim 2
Dependent Claim
209 words
In a process for upgrading tar sands by the combination of thermal distillation to recover a distillate material boiling below about 850° F. and gasification of residue hydrocarbonaceous material remaining with the sand recovered from the thermal distillation operation to produce fuel gas and high temperature streams of sand particles, air and steam transferable for use in the process combination, the improvement which comprises effecting thermal distillation of tar sand admixed with hot sand particles obtained from said gasification step under conditions to obtain a hydrocarbon product of end boiling point within the range of 650° F. to about 1000° F., passing sand with residual oily higher boiling hydrocarbon material from said thermal distillation operation to a solvent extraction operation maintained under conditions to remove said higher boiling hydrocarbons other than asphaltic type organic material by solvent extraction, passing sand with asphaltic type organic material separated from solvent extracted material to said gasification zone maintained under conditions to produce a fuel gas product and hot sand particles, recovering solvent with extracted higher boiling hydrocarbons and separating to recover solvent from said higher boiling hydrocarbons, and using the hot fuel gas product and sand obtained from said gasification operation to provide heat to the above identified combination of processing steps.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the end point of the hydrocarbon material recovered by thermal distillation is about 690° F.
Claim 4
Dependent Claim
21 words
The process of claim 1 wherein the end point of the hydrocarbon material recovered by thermal distillation is about 800° F.
Claim 5
Dependent Claim
21 words
The process of claim 1 wherein the end point of the hydrocarbon material recovered by thermal distillation is about 950° F.
Claim 6
Dependent Claim
37 words
The process of claim 2 wherein light gas oil and lower boiling hydrocarbons including kerosine and gasoline are recovered by said thermal distillation and recovered higher boiling hydrocarbons by solvent extraction are used to produce lube oils.
Claim 7
Dependent Claim
19 words
The process of claim 2 wherein material higher boiling than a heavy gas oil is recovered by solvent extraction.
Claim 8
Dependent Claim
25 words
The process of claim 1 wherein hot sand particles recovered from the gasification step are partially cooled prior to charging to the thermal distillation operation.
Claim 9
Dependent Claim
36 words
The process of claim 1 wherein sand particles comprising an asphaltic residue are admixed with hot particles of sand from said gasification step before transfer to said gasification step by a riser or by a standpipe.
Claim 10
Dependent Claim
28 words
The process of claim 1 wherein the solvent with hydrocarbon extract is recycled through the solvent extraction zone more than once before separation of solvent from hydrocarbon extract.
Claim 11
Dependent Claim
26 words
The process of claim 1 wherein the solvent extraction zone is positioned above the gasification zone and the gasification zone is beneath the thermal distillation zone.
References Cited (Backward Citations)
US3118741A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-04-08 | 1983-10-08 | 1984-04-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-04-08 | 1987-10-08 | 1988-04-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-04-08 | 1991-10-08 | 1992-04-08 | $7700.00 | Window Closed / Lapsed |