Process for upgrading a hydrocarbon fraction

• US 3,960,708 A
• Filed: 05/31/1974
• Issued: 06/01/1976
• Est. Priority Date: 05/31/1974
• Status: Expired due to Term

• Current Assignee: Standard Oil Company (BP PLC)
• Original Assignee: Standard Oil Company (BP PLC)
• Inventors: Quick, Leonard M., McCollum, John D.
• Primary Examiner(s): Gantz, Delbert E.
• Assistant Examiner(s): Schmitkons, G. E.
• Application Number:
  US05/474,913
• Time in Patent Office: 732 Days
• Field of Search: 208/121, 208/112, 208/216-217, 208/251, 208/108, 208/110-111, 208/208 R, 208/254
• US Class Current: 208/121
• CPC Class Codes: C10G 1/00 Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal mechanical winning of oil from oil-shales, oil-sand, or the like B03B
• CPC Class Codes: C10G 1/04 by extraction
• CPC Class Codes: C10G 1/083 in the presence of a solvent

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

Claims

1. 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.

2. The process of claim 1 wherein the density of water in the water-containing fluid is at least 0.15 gram per milliliter.

3. The process of claim 2 wherein the density of water in the water-containing fluid is at least 0.2 gram per milliliter.

4. The process of claim 1 wherein the temperature is at least 705°

F.

5. 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.

6. 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.

7. 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.

8. 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.

9. 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.

10. 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.

11. 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.

12. 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.

13. The process of claim 1 wherein the water-containing fluid is water.

14. 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.

15. 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.

16. 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.

17. The process of claim 1 wherein the water-containing fluid is substantially water.