Patent US3948755A successfully refreshed from Google Patents.
US3948755A
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Process for recovering and upgrading hydrocarbons from oil shale and tar sands
Assignee: Standard Oil Co
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Filing: 1974-05-31
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Granted: 1976-04-06
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Expires: 1994-05-31
Abstract
Abstract A process for recovering and upgrading hydrocarbons from oil shale and tar sands by contacting the oil shale or tar sands with a dense-water-containing fluid at a temperature in the range of from about 600°F. to about 900°F. in the absence of externally supplied hydrogen and in the presence of a sulfur-resistant catalyst and wherein the density of the water in said fluid is at least 0.10 gram per milliliter.
Inventors
- 👤 John D. McCollum
- 👤 Leonard M. Quick
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 14:27
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/083; C10G1/04; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 21
Claim 1
Independent Claim
221 words
A process for recovering hydrocarbons from oil shale or tar sands solids and simultaneously for cracking, desulfurizing, and demetalating the recovered hydrocarbons, comprising contacting the oil shale or tar sands solids with a water-containing fluid under superatmospheric pressure, at a temperature in the range of from about 600°F. to about 900°F., in the absence of externally supplied hydrogen, and in the presence of an externally supplied, sulfur-resistant catalyst, selected from the group consisting of at least one basic metal carbonate, basic metal hydroxide, transition metal oxide, oxide-forming transition metal salt, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein the transition metal in the oxide and salt is selected from the group consisting of the transition metals of Groups IVB, VB, VIB, and VIIB; wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of alkali metals; wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.10 gram per milliliter and serves as an effective solvent for the recovered hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for such hydrocarbons and to thereby form separate phase.
Claim 2
Dependent Claim
221 words
A process for recovering hydrocarbons from oil shale or tar sands solids and simultaneously for cracking, desulfurizing, and demetalating the recovered hydrocarbons, comprising contacting the oil shale or tar sands solids with a water-containing fluid under superatmospheric pressure, at a temperature in the range of from about 600°F. to about 900°F., in the absence of externally supplied hydrogen, and in the presence of an externally supplied, sulfur-resistant catalyst, selected from the group consisting of at least one basic metal carbonate, basic metal hydroxide, transition metal oxide, oxide-forming transition metal salt, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein the transition metal in the oxide and salt is selected from the group consisting of the transition metals of Groups IVB, VB, VIB, and VIIB; wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of alkali metals; wherein sufficient water is present in the water-containing fluid and said pressure is sufficiently high so that the water in the water-containing fluid has a density of at least 0.10 gram per milliliter and serves as an effective solvent for the recovered hydrocarbons; and lowering said temperature or pressure or both, to thereby make the water in the water-containing fluid a less effective solvent for such hydrocarbons and to thereby form separate phase.
Claim 3
Dependent Claim
21 words
The process of claim 1 wherein the density of water in the water-containing fluid is at least 0.15 gram per milliliter.
Claim 4
Dependent Claim
21 words
The process of claim 2 wherein the density of water in the water-containing fluid is at least 0.2 gram per milliliter.
Claim 5
Dependent Claim
12 words
The process of claim 1 wherein the temperature is at least 705°F.
Claim 6
Dependent Claim
36 words
The process of claim 1 wherein the oil shale or tar sands solids are contacted with the water-containing fluid for a period of time in the range of from about 1 minute to about 6 hours.
Claim 7
Dependent Claim
36 words
The process of claim 5 wherein the oil shale or tar sands solids are contacted with the water-containing fluid for a period of time in the range of from about 5 minutes to about 3 hours.
Claim 8
Dependent Claim
36 words
The process of claim 6 wherein the oil shale or tar sands solids are contacted with the water-containing fluid for a period of time in the range of from about 10 minutes to about 1 hour.
Claim 9
Dependent Claim
31 words
The process of claim 1 wherein the weight ratio of oil shale or tar sand solids-to-water in the water-containing fluid is in the range of from about 3:2 to about 1:10.
Claim 10
Dependent Claim
31 words
The process of claim 8 wherein the weight ratio of oil shale or tar sand solids-to-water in the water-containing fluid is in the range of from about 1:1 to about 1:3.
Claim 11
Dependent Claim
12 words
The process of claim 1 wherein the water-containing fluid is substantially water.
Claim 12
Dependent Claim
11 words
The process of claim 1 wherein the water-containing fluid is water.
Claim 13
Dependent Claim
19 words
The process of claim 1 wherein the oil shale solids have a maximum particle size of one-half inch diameter.
Claim 14
Dependent Claim
19 words
The process of claim 12 wherein the oil shale solids have a maximum particle size of one-quarter inch diameter.
Claim 15
Dependent Claim
18 words
The process of claim 13 wherein the oil shale solids have a maximum particle size of 8 mesh.
Claim 16
Dependent Claim
32 words
The process of claim 1 wherein the transition metal in the oxide and salt is selected from the group consisting of vanadium, chromium, manganese, titanium, molybdenum, zirconium, niobium, tantalum, rhenium, and tungsten.
Claim 17
Dependent Claim
26 words
The process of claim 15 wherein the transition metal in the oxide and salt is selected from the group consisting of chromium, manganese, titanium, and tungsten.
Claim 18
Dependent Claim
25 words
The process of claim 1 wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of sodium and potassium.
Claim 19
Dependent Claim
41 words
The process of claim 1 wherein the catalyst is present in a catalytically effective amount which is equivalent to a concentration level in the water in the water-containing fluid in the range of from about 0.01 to about 3.0 weight percent.
Claim 20
Dependent Claim
41 words
The process of claim 18 wherein the catalyst is present in a catalytically effective amount which is equivalent to a concentration level in the water in the water-containing fluid in the range of from about 0.10 to about 0.50 weight percent.
Claim 21
Dependent Claim
21 words
The process of claim 1 wherein essentially all the sulfur removed the recovered hydrocarbons is in the form of elemental sulfur.
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) | 1979-04-06 | 1979-10-06 | 1980-04-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-04-06 | 1983-10-06 | 1984-04-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-04-06 | 1987-10-06 | 1988-04-06 | $7700.00 | Window Closed / Lapsed |