IP Library Patent Application 14104711
Patent Application
App. No. 14/104,711

STEAM ASSISTED GRAVITY DRAINAGE WITH ADDED OXYGEN ("SAGDOX") IN DEEP RESERVOIRS

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 None
App. No.
14/104,711
Abstract

A process to recover hydrocarbons, from a hydrocarbon reservoir having a bottom, using a substantially horizontal production well, the substantially horizontal production well having a toe and a heel, the process including: (a) injecting oxygen into the hydrocarbon reservoir, the horizontal production well having at least one perforation zone for contact with the reservoir; (b) injecting steam into the hydrocarbon reservoir; the oxygen producing in situ heat and in situ carbon dioxide by combustion and the steam producing in situ heat by conduction and condensation; the in situ carbon dioxide dissolving into the liquid hydrocarbon, lowering its viscosity; (c) recovering the reservoir liquid hydrocarbons of lowered viscosity using the substantially horizontal production well; and (d) optionally conveying the recovered liquid hydrocarbons to the surface; where the process is absent a removal step of any non-condensable gas from the reservoir.

Claims (31)

1 . A process to recover hydrocarbons, from a hydrocarbon reservoir having a bottom, using a substantially horizontal production well, said substantially horizontal production well having a toe and a heel, said process comprising:

(a) injecting oxygen into said hydrocarbon reservoir, said horizontal production well having at least one perforation zone for contact with said reservoir;

(b) injecting steam into said hydrocarbon reservoir; said oxygen producing in situ heat and in situ carbon dioxide by combustion and said steam producing in situ heat by conduction and condensation; said in situ carbon dioxide dissolving into the liquid hydrocarbon, lowering its viscosity;

(c) recovering said reservoir liquid hydrocarbons of lowered viscosity using said substantially horizontal production well; and

(d) optionally conveying said recovered liquid hydrocarbons to the surface;

wherein said process is absent a removal step of any non-condensable gas from said reservoir.

2 . The process of claim 2 wherein said hydrocarbon reservoir comprises at least one characteristic selected from the group consisting of:

(a) an average depth greater than about 500 metres;

(b) an average pressure greater than about 800 psia, and combinations thereof.

3 . A process to recover liquid hydrocarbons, from a hydrocarbon reservoir having a bottom, using a horizontal production well, comprising:

(a) Completing the horizontal production well within 2 metres of the reservoir bottom;

(b) injecting oxygen gas into the hydrocarbon reservoir within 50 metres from the horizontal production well and with a perforation (reservoir contact) zone less than 50 metres in length;

(c) injecting steam within 20 metres from the horizontal production well;

(d) the oxygen gas producing in situ heat and in situ carbon dioxide by combustion and the steam producing in situ heat by conduction and by condensation;

(e) said carbon dioxide dissolving into the reservoir hydrocarbon, lowering its viscosity;

(f) in situ heat causing the liquid hydrocarbon to be heated, also lowering its viscosity;

(g) the lower-viscosity reservoir liquid hydrocarbon draining by gravity to the horizontal production well where it is conveyed (or pumped) to the surface; and

(h) the process pressure (in the reservoir) is greater than 800 psia.

4 . A process according to claim 1 or 3 , wherein oxygen to steam injected is controlled so that produced water to oil (v/v liquid) has a ratio greater than 0.5.

5 . A process according to claim 4 , wherein the ratio of produced water to oil (v/v liquid) is between 0.5 and 2.0.

6 . A process according to claim 3 , wherein said hydrocarbon reservoir is positioned at least 500 metres below a ground surface.

7 . A process according to claim 3 , wherein steam is injected within 10 metres from the horizontal production well.

8 . A process according to claim 1 or 7 , wherein steam is injected using a substantially parallel horizontal well to the horizontal production well and located about 3 metres to 8 metres above the horizontal production well.

9 . A process according to claim 1 or 7 , wherein steam is injected into the reservoir using at least one well selected from the group consisting of a single substantially vertical well or a plurality of substantially vertical wells.

10 . A process according to claim 1 , wherein the oxygen is injected into the reservoir using at least one well selected from the group consisting of a single substantially vertical well or a plurality of substantially vertical wells.

11 . A process according to claim 9 , wherein steam and oxygen are comingled on the surface and injected into the reservoir.

12 . A process according to claim 10 , wherein steam and oxygen are segregated and injected separately into the reservoir.

13 . A process according to claim 12 wherein said steam and oxygen are segregated using concentric tubing and packers with steam in a central tubing of said concentric tubing surrounded by oxygen in an adjacent annulus and said oxygen is injected at a higher elevation of said steam injected into the reservoir.

14 . A process according to claim 13 , wherein said steam and oxygen are injected into said reservoir using a single substantially vertical well, wherein said single substantially vertical well is completed within 50 metres from the toe of the horizontal production well.

15 . A process according to claim 1 or 3 wherein said reservoir has a pressure such that substantially no free CO 2 is produced in the production well.

16 . A process according to claim 1 or 3 wherein said process has an operating in situ pressure and an oxygen/steam (v/v) ratio such that the substantially horizontal production well is substantially free of free CO 2 .

Assignments (4)
CHANGE OF NAME Recorded Feb 19, 2019
From: NEXEN ENERGY ULC
To: CNOOC PETROLEUM NORTH AMERICA ULC
Reel/Frame 048366/0576 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 12, 2013
From: KERR, RICHARD KELSO
To: NEXEN INC.
Reel/Frame 031774/0497 →
CHANGE OF NAME Recorded Dec 12, 2013
From: NEXEN ENERGY INC.
To: NEXEN ENERGY ULC
Reel/Frame 031774/0782 →
CERTIFICATE OF COVERAGE Recorded Dec 12, 2013
From: NEXEN INC.
To: NEXEN ENERGY INC.
Reel/Frame 031805/0868 →