UPGRADING HEAVY HYDROCARBON OILS

• US 20080099376A1
• Filed: 10/31/2006
• Published: 05/01/2008
• Est. Priority Date: 10/31/2006
• Status: Abandoned Application

• Current Assignee: Chevron USA Incorporated (Chevron Corp.)
• Original Assignee: Chevron USA Incorporated (Chevron Corp.)
• Inventors: Li, Lin, Li, Lixiong, He, Zunqing, Chinn, Daniel
• Application Number:
  US11/555,048
• Publication Number:
  US 20080099376A1
• Time in Patent Office: Days
• US Class Current: 208/264
• CPC Class Codes: C10G 31/08 by treating with water

Abstract

A process using supercritical water to upgrade a heavy hydrocarbon feedstock into an upgraded hydrocarbon product or syncrude with highly desirable properties (low sulfur content, low metals content, lower density (higher API), lower viscosity, lower residuum content, etc.) is disclosed. The process does not require external supply of hydrogen nor does it use externally supplied catalysts.

Claims

1. A process for upgrading hydrocarbons comprising,

(a) mixing hydrocarbons with a fluid comprising water in a mixing zone to form a mixture;

(b) passing the mixture to a reaction zone;

(c) reacting the mixture in the reaction zone under supercritical water conditions in the absence of externally added hydrogen for a residence time sufficient to allow upgrading reactions to occur;

(d) withdrawing a single-phase reaction product from the reaction zone; and

(e) separating the reaction product into gas, effluent water, and upgraded hydrocarbon phases.

2. A process according to claim 1, wherein the hydrocarbons are heavy hydrocarbons selected from the group consisting of whole heavy petroleum crude oil, tar sand bitumen, heavy hydrocarbon fractions obtained from crude petroleum oils, heavy vacuum gas oils, vacuum residuum, petroleum tar, coal tar and their mixtures.

3. A process according to claim 1, wherein the fluid comprising water enters the mixing zone at a temperature greater than the critical temperature of water.

4. A process according to claim 1, wherein the conditions in the mixing zone include a temperature higher than the critical temperature of water and a pressure greater than the critical pressure of water.

5. A process according to claim 1, wherein the supercritical water conditions include a temperature from 374°

C. to 1000°

C. a pressure from 3,205 psia to 10,000 psia an oil/water volume ratio from 1;

0.1 to 1;

10 and where the residence time is from 1 minute to 6 hours.

6. A process according to claim 1, wherein the supercritical water conditions include a temperature from 374°

C. to 600°

C., a pressure from 3,205 psia to 7,200 psia, an oil/water volume ratio from 1;

0.5 to 1;

3 and where the residence time is from 8 minutes to 2 hours.

7. A process according to claim 1, wherein the supercritical water conditions include a temperature from 374°

C. to 400°

C., a pressure from 3,205 psia to 4,000 psia, an oil/water volume ratio from 1;

1 to 1;

2 and where the residence time is from 20 to 40 minutes.

8. A process according to claim 1 wherein the mixture in the reaction zone is reacted in the absence of any catalyst or promoter.

9. A process according to claim 1, wherein the water is drinking water, treated wastewater, untreated wastewater, river water, lake water, seawater, produced water or their mixtures.

10. A process for upgrading hydrocarbons comprising:

(a) mixing hydrocarbons with a fluid comprising water in a mixing zone to form a mixture;

(b) passing the mixture to a reaction zone;

(c) reacting the mixture in the reaction zone under supercritical water conditions in the absence of externally added hydrogen and catalyst for a residence time sufficient to allow upgrading reactions to occur;

(d) withdrawing a single-phase reaction product from the reaction zone; and

(e) separating the reaction product into gas, effluent water, and upgraded hydrocarbon phases.

11. A process according to claim 10, wherein the hydrocarbons are heavy hydrocarbons selected from the group consisting of whole heavy petroleum crude oil, tar sand bitumen, heavy hydrocarbon fractions obtained from crude petroleum oils, heavy vacuum gas oils, vacuum residuum, petroleum tar, coal tar and their mixtures.

12. A process according to claim 10, wherein the fluid comprising water enters the mixing zone at a temperature greater than the critical temperature of water.

13. A process according to claim 10, wherein the conditions in the mixing zone include a temperature greater than the critical temperature of water and a pressure greater than the critical pressure of water.

14. A process according to claim 10, wherein the supercritical water conditions include a temperature from 374°

C. to 1000°

C., a pressure from 3,205 psia to 10,000 psia, an oil/water volume ratio from 1;

0.1 to 1;

10 and where the residence time is from 1 minute to 6 hours.

15. A process according to claim 10, wherein the supercritical water conditions;

include a temperature from 374°

C. to 600°

C., a pressure from 3,205 psia to 7,200 psia, an oil/water volume ratio from 1;

0.5 to 1;

3 and where the residence time is from 8 minutes to 2 hours.

16. A process according to claim 10, wherein the supercritical water conditions include a temperature from 374°

C. to 400°

C. a pressure from 3,205 psia to 4,000 psia, an oil/water volume ratio from 1;

1 to 1;

2 and where the residence time is from 20 to 40 minutes.

17. A process according to claim 10, wherein the water is drinking water, treated wastewater, untreated wastewater, river water, lake water, seawater, produced water or their mixtures.