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US3960708A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for upgrading a hydrocarbon fraction

Assignee: Standard Oil Co
•
Filing: 1974-05-31
•
Granted: 1976-06-01
•
Expires: 1994-05-31
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Abstract

Abstract A process for upgrading a hydrocarbon fraction by contacting the hydrocarbon fraction 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 of pretreatment of the hydrocarbon fraction and in the presence of a sulfur-resistant catalyst. RELATED APPLICATIONS

Inventors

  • 👤 John D. McCollum
  • 👤 Leonard M. Quick

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 09:48
CPC Classifications
C; C10; C10G; C10G1/00; C10G1/08; C10G1/083; C10G1/04

Claims Analysis

Total Claims: 18
Claim 1
Independent Claim 245 words
A process for cracking, desulfurizing, and demetalating a hydrocarbon fraction containing paraffins, olefins, olefin-equivalents, or acetylenes, as such or as substituents on ring compounds, and sulfurous and metallic components: comprising cracking, desulfurizing, and demetalating said hydrocarbon fraction by contacting said hydrocarbon fraction with a water-containing fluid at a temperature in the range of from about 600°F. to about 900°F., under super-atmospheric pressure, 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 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 a transition metal of Group IVB, VB, VIB, and VIIB of the Periodic Chart, and 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 hydrocarbon fraction; and lowering said temperature or pressure or both to thereby make the water in the water-containing fluid a less effective solvent for the hydrocarbon fraction and to thereby form separate phases, wherein essentially all the sulfur separated from the hydrocarbon fraction is in the form of elemental sulfur.
Claim 2
Dependent Claim 245 words
A process for cracking, desulfurizing, and demetalating a hydrocarbon fraction containing paraffins, olefins, olefin-equivalents, or acetylenes, as such or as substituents on ring compounds, and sulfurous and metallic components: comprising cracking, desulfurizing, and demetalating said hydrocarbon fraction by contacting said hydrocarbon fraction with a water-containing fluid at a temperature in the range of from about 600°F. to about 900°F., under super-atmospheric pressure, 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 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 a transition metal of Group IVB, VB, VIB, and VIIB of the Periodic Chart, and 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 hydrocarbon fraction; and lowering said temperature or pressure or both to thereby make the water in the water-containing fluid a less effective solvent for the hydrocarbon fraction and to thereby form separate phases, wherein essentially all the sulfur separated from the hydrocarbon fraction is in the form of elemental sulfur.
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 31 words
The process of claim 1 wherein the hydrocarbon fraction and water-containing fluid are contacted for a period of time in the range of from about 1 minute to about 6 hours.
Claim 7
Dependent Claim 30 words
The process of claim 5 wherein the hydrocarbon fraction and water-containing fluid are contacted for a period of time in the range of from about 5 to about 3 hours.
Claim 8
Dependent Claim 31 words
The process of claim 6 wherein the hydrocarbon fraction and water-containing fluid are contacted for a period of time in the range of from about 10 minutes to about 1 hour.
Claim 9
Dependent Claim 26 words
The process of claim 1 wherein the weight ratio of hydrocarbon fraction-to-water in the water-containing fluid is the range of from about 1:1 to about 1:10.
Claim 10
Dependent Claim 27 words
The process of claim 6 wherein the weight ratio of hydrocarbon fraction-to-water in the water-containing fluid is in the range of from about 1:2 to about 1:3.
Claim 11
Dependent Claim 24 words
The process of claim 1 wherein the hydrocarbon fraction is contacted with the water-containing fluid in the absence of pretreatment of the hydrocarbon fraction.
Claim 12
Dependent Claim 34 words
The process of claim 1 wherein the transition metal in the oxide and salt is selected from the group consisting of vanadium, chromiun, manganese, iron, titanium, molybdenum, copper, zirconium, niobium, tantalum, rhenium, and tungsten.
Claim 13
Dependent Claim 27 words
The process of claim 11 wherein the transition metal in the oxide and salt is selected from the group consisting of chromium, mangenese, titanium, tantalum, and tungsten.
Claim 14
Dependent Claim 11 words
The process of claim 1 wherein the water-containing fluid is water.
Claim 15
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 16
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 17
Dependent Claim 41 words
The process of claim 15 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 18
Dependent Claim 12 words
The process of claim 1 wherein the water-containing fluid is substantially water.

References Cited (Backward Citations)

US2211944A Cited
US3453206A Cited
US3586621A Cited
US3501396A Cited
US3676331A Cited
US3687838A Cited

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

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