US3948754A
Expired / Lapsed
US
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Process for recovering and upgrading hydrocarbons from oil shale and tar sands
Assignee: Standard Oil Co
•
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 supplied hydrogen and in the presence of a sulfur- and nitrogen-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
2026-11-04 05:33
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/083; C10G1/04; Y; Y10; Y10S; Y10S208/00; Y10S208/952
Claims Analysis
Total Claims: 26
Claim 1
Independent Claim
211 words
A process for recovering hydrocarbons from oil shale or tar sands solids and simultaneously for cracking, hydrogenating, desulfurizing, demetalating, and dentrifying the recovered hydrocarbons, comprising contacting the oil shale or tar sands solids with a water-containing fluid under super-atmospheric 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 catalyst system containing a sulfur- and nitrogen-resistant catalyst selected from the group consisting of at least one soluble or insoluble transition metal compound, a transition metal deposited on a support, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein said transition metal in said catalyst is selected from the group consisting of ruthenium, rhodium, iridium, osmium, palladium, nickel, cobalt, platinum, and combinations thereof, 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 phases.
Claim 2
Dependent Claim
211 words
A process for recovering hydrocarbons from oil shale or tar sands solids and simultaneously for cracking, hydrogenating, desulfurizing, demetalating, and dentrifying the recovered hydrocarbons, comprising contacting the oil shale or tar sands solids with a water-containing fluid under super-atmospheric 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 catalyst system containing a sulfur- and nitrogen-resistant catalyst selected from the group consisting of at least one soluble or insoluble transition metal compound, a transition metal deposited on a support, and combinations thereof, wherein said catalyst is present in a catalytically effective amount, wherein said transition metal in said catalyst is selected from the group consisting of ruthenium, rhodium, iridium, osmium, palladium, nickel, cobalt, platinum, and combinations thereof, 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 phases.
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
13 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
30 words
The process of claim 1 wherein the ratio of oil shale or tar sands 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 sands 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
26 words
The process of claim 1 wherein the transition metal in the catalyst is selected from the group consisting of ruthenium, rhodium, iridium, osmium, and combinations thereof.
Claim 17
Dependent Claim
38 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-containing fluid in the range of from about 0.02 to about 1.0 weight percent.
Claim 18
Dependent Claim
38 words
The process of claim 16 wherein the catalyst is present in a catalytically effective amount which is equivalent to a concentration level in the water-containing fluid in the range of from about 0.05 to about 0.15 weight percent.
Claim 19
Dependent Claim
97 words
The process of claim 1 wherein the catalyst system contains additionally a promoter selected from the group consisting of at least one basic metal hydroxide, basic metal carbonate, transition metal oxide, oxide-forming transition metal salt, and combinations thereof, wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of alkali metals, 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 of the Periodic Chart, and wherein said promoter promotes the activity of the catalyst.
Claim 20
Dependent Claim
32 words
The process of claim 18 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 21
Dependent Claim
27 words
The process of claim 19 wherein the transition metal in the oxide and salt is selected from the group consisting of chromium, manganese, titanium, tantalum, and tungsten.
Claim 22
Dependent Claim
25 words
The process of claim 18 wherein the metal in the basic metal carbonate and hydroxide is selected from the group consisting of sodium and potassium.
Claim 23
Dependent Claim
39 words
The process of claim 18 wherein the ratio of the number of atoms of metal in the promoter to the number of atoms of metal in the catalyst is in the range of from about 0.5 to about 50.
Claim 24
Dependent Claim
39 words
The process of claim 22 wherein the ratio of the number of atoms of metal in the promoter to the number of atoms of metal in the catalyst is in the range of from about 3 to about 5.
Claim 25
Dependent Claim
22 words
The process of claim 1 wherein essentially all the sulfur removed from the recovered hydrocarbons is in the form of elemental sulfur.
Claim 26
Dependent Claim
11 words
The process of claim 1 wherein hydrogen is generated in situ.
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 |