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US3948754A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for recovering and upgrading hydrocarbons from oil shale and tar sands

Assignee: Standard Oil Co
•
Filing: 1974-05-31
•
Granted: 1976-04-06
•
Expires: 1994-05-31
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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)

US3116234A Cited
US3586621A Cited
US3501396A Cited
US3725495A Cited
US3676331A Cited

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

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