Process for producing and separating oil

Patent metadata

Field	Value
Publication number	US-9540574-B2
Application number	US-201313961366-A
Country	US
Kind code	B2
Filing date	Aug 7, 2013
Priority date	Aug 9, 2012
Publication date	Jan 10, 2017
Grant date	Jan 10, 2017

Abstract

The present invention is directed to a process for producing and separating oil. An aqueous fluid having an ionic content of at most 0.15 M and a total dissolved solids content of from 200 ppm to 10,000 ppm is introduced into an oil-bearing formation. Oil and water are produced from the formation subsequent to the introduction of the aqueous fluid into the formation. A demulsifier and a brine solution having a total dissolved solids content of greater than 10,000 ppm are mixed with the oil and water produced from the formation. Oil is then separated from the mixture of oil, water, demulsifier, and brine solution.

First claim

What is claimed is:

1. A process for producing oil, comprising
contacting a source water having a total dissolved solids content of at least 10,000 ppm with a first ionic filter which first ionic filter is a nanofiltration membrane, a reverse osmosis membrane or a forward osmosis membrane;
passing a portion of the source water through the first ionic filter to form a permeate having reduced salinity relative to the source water while excluding at least a portion of the source water from passing through the first ionic filter to form a primary retentate having increased salinity relative to the source water due to passing the portion of the source water through the first ionic filter;
passing a portion of the permeate through one or more second ionic filters wherein the one or more second ionic filters are selected from the group consisting of a nanofiltration membrane, a reverse osmosis membrane, a forward osmosis membrane and combinations thereof, to form a treated water having reduced salinity relative to the permeate while excluding at least a portion of the permeate from passing through the one or more second ionic filters to form one or more secondary retentates having increased salinity relative to the permeate due to passing the portion of the permeate through the one or more second ionic filters;
utilizing the treated water as at least a portion of an aqueous fluid injected into the formation which aqueous fluid has an ionic strength of at most 0.15 M and a total dissolved solids content of from 200 ppm to 10,000 ppm into an oil-bearing formation;
producing oil and water from the formation subsequent to the introduction of the aqueous fluid into the formation;
mixing a demulsifier and a brine solution having a total dissolved solids content of greater than 10,000 ppm with at least a portion of the oil and water produced from the formation wherein at least a portion of the brine solution is primary retentate, one or more of the secondary retentates, or a combination of the primary retentate and one or more of the secondary retentates; and
separating oil from the mixture of oil, water, demulsifier, and brine solution.

2. The process of claim 1 wherein the brine solution has a total dissolved solids content of at least 15,000 ppm, or at least 20,000 ppm, or at least 25,000 ppm, or at least 30,000 ppm, or at least 40,000 ppm, or at least 50,000 ppm.

3. The process of claim 1 wherein the brine solution is selected from seawater, brackish water, or production water produced from the formation.

4. The process of claim 1 wherein from 0.2 up to 1 pore volume of the low salinity aqueous fluid is introduced into the formation.

5. The process of claim 1 , further comprising the step of introducing a drive fluid into the formation subsequent to introducing the low salinity aqueous fluid into the formation.

6. The process of claim 1 wherein the oil-bearing formation further comprises connate water having a divalent ion concentration, wherein the low salinity aqueous fluid has a divalent ion concentration, and wherein the divalent ion concentration of the aqueous fluid is less than the divalent ion concentration of the connate water.

7. The process of claim 1 wherein the low salinity aqueous fluid is water from an aquifer, a lake or a river.

8. The process of claim 1 wherein the water produced from the formation comprises water that is emulsified with at least a portion of the oil produced from the formation and free water that is separable from the oil produced from the formation absent demulsification, and oil produced from the formation comprises oil that is emulsified with at least a portion of the water produced from the formation and free oil that is separable from the water produced from the formation absent demulsification, further comprising the step of separating the free water and the free oil from the emulsified oil and emulsified water prior to mixing the brine solution with the oil and water produced from the formation.

9. The process of claim 1 wherein the source water is selected from the group consisting of seawater, brackish water, water produced from the formation, water from the mixture of oil, water and brine solution subsequent to separation of oil from the mixture, and combinations thereof.

10. The process of claim 8 or 9 further comprising the step of pressurizing the source water to a pressure of from 2.0 MPa (300 psia) to 9.0 MPa (1,300 psia) prior to contacting the source water with the ionic filter.

11. The process of claim 1 wherein the source water is selected from the group consisting of seawater, brackish water, water produced from the formation, water from the mixture of oil, water, and brine solution subsequent to separation of oil from the mixture, and combinations thereof.

12. The process of claim 1 further comprising the step of pressurizing the source water to a pressure of from 2 MPa (300 psia) to 9 MPa (1,300 psia) prior to contacting the source water with the first ionic filter.

13. The process of claim 1 wherein the oil-bearing formation is a subterranean sandstone formation comprising a mineral having a negative zeta potential.

14. The process of claim 1 wherein the oil-bearing formation is a subterranean carbonate formation comprised of microcrystalline limestone, dolomite, or a mixture thereof.

Assignees

• Shell Oil Co

Inventors

• Janssen Albert Joseph Hendrik
• Suijkerbuijk Bartholomeus Marinus Josephus Maria

Classifications

• C10G33/04 Primary

  with chemical means · CPC title

• E21B43/35

  specially adapted for separating solids (down-hole drilling fluid separation systems E21B21/002; separating solids from drilling fluids E21B21/065) · CPC title

• C09K8/035

  Organic additives · CPC title

• E21B43/20 Primary

  Displacing by water · CPC title

• E21B43/34

  Arrangements for separating materials produced by the well · CPC title