IP Library Granted Patent US 7,922,895
Granted Patent B2
US 7,922,895 · App. 12/633,232 · Granted Apr 12, 2011

Supercritical water processing of extra heavy crude in a slurry-phase up-flow reactor system

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 7,922,895
App. No.
12/633,232
Granted
Apr 12, 2011
Kind
B2
Abstract

A method of mixing a catalyst with a heavy oil to create a heavy oil/catalyst mixture. This is followed by combining the heavy oil/catalyst mixture with supercritical water to form light hydrocarbon products and heavy hydrocarbon products. By doing so the light hydrocarbon products can be separated into a gaseous top product, an upgraded liquid hydrocarbon product and a water phase.

Claims (13)

1. A method comprising:

a) mixing a catalyst with a heavy oil to create a heavy oil/catalyst mixture; and

b) combining the heavy oil/catalyst mixture with supercritical water to form light hydrocarbon products and heavy hydrocarbon products;

wherein the light hydrocarbon products can be separated into a gaseous top product, an upgraded liquid hydrocarbon product and a water phase;

wherein the catalyst is zirconium oxide that is promoted with an alkali salt that is present in an amount of about 1% of the zirconium oxide.

2. The method of claim 1 , wherein the heavy oil has an API less than 10.

3. The method of claim 1 , wherein the upgraded liquid hydrocarbon product has an API greater than 19.

4. The method of claim 1 , wherein the heavy oil has a viscosity greater than half million cSt at 60° F.

5. The method of claim 1 , wherein the upgraded liquid hydrocarbon product has a viscosity lower than 350 cSt at 60° F.

6. The method of claim 1 , wherein the upgraded liquid hydrocarbon has a nitrogen content less than 100 ppm.

7. The method of claim 1 , wherein the gaseous top product contains C1-C4, H 2 S, CO, CO 2 and H 2 .

8. The method of claim 1 , wherein a portion of the supercritical water comprises from recycling the water phase.

9. The method of claim 1 , wherein the supercritical water contains added CO.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 15, 2012
From: CONOCOPHILLIPS COMPANY
To: PHILLIPS 66 COMPANY
Reel/Frame 028213/0824 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 8, 2009
From: BANERJEE, DWIJEN K.
To: CONOCOPHILLIPS COMPANY
Reel/Frame 023621/0202 →