Method of controlling salinity of a low salinity injection water

Patent metadata

Field	Value
Publication number	US-11407654-B2
Application number	US-201816628633-A
Country	US
Kind code	B2
Filing date	Jul 12, 2018
Priority date	Jul 12, 2017
Publication date	Aug 9, 2022
Grant date	Aug 9, 2022

Abstract

An integrated system includes a desalination plant including a reverse osmosis (RO) array to produce an RO permeate blending stream and a nanofiltration (NF) array to produce an NF permeate blending stream. The integrated system also includes a blending system. Further, the integrated system includes a control unit. Still further, the integrated system includes an injection system for one or more injection wells that penetrate an oil-bearing layer of a reservoir. Moreover, the integrated system includes a production facility to separate fluids produced from one or more production wells that penetrate the oil-bearing layer of the reservoir and to deliver a produced water (PW) stream to the blending system. The blending system is configured to blend the RO permeate and NF permeate blending streams with the PW stream to produce a blended low salinity water stream. The control unit is configured to dynamically alter operation of the blending system to adjust amounts of at least one of the RO permeate blending stream and the NF permeate blending stream to maintain a composition of the blended low salinity water stream within a predetermined operating envelope.

First claim

The invention claimed is:

1. An integrated system comprising:
a desalination plant comprising a reverse osmosis (RO) array configured to produce an RO permeate blending stream and a nanofiltration (NF) array configured to produce an NF permeate blending stream;
a blending system;
a control unit;
an injection system for one or more injection wells, wherein the one or more injection wells penetrate an oil-bearing layer of a reservoir; and
a production facility configured to: separate fluids produced from one or more production wells that penetrate the oil-bearing layer of the reservoir and deliver a produced water (PW) stream to the blending system,
wherein the blending system is configured to blend the RO permeate and the NF permeate blending streams with the PW stream to produce a blended low salinity water stream,
wherein the control unit is configured to:
dynamically alter operation of the blending system to adjust amounts of at least one of the RO permeate blending stream or the NF permeate blending stream to maintain a composition of the blended low salinity water stream within a predetermined operating envelope; and
dynamically adjust amounts of at least one of the RO permeate discharged from the blending system via an RO permeate dump line or the NF permeate discharged from the blending system via an NF permeate dump line.

2. The integrated system of claim 1 , wherein the control unit is configured to receive the operating envelope from a source external to the control unit.

3. The integrated system of any one of the preceding claims, wherein the operating envelope specifies upper and lower limits for a parameter selected from the group consisting of: total dissolved solids (TDS) content; ionic strength; concentrations of individual ions; concentration of types of individual ions; ratios of types of individual ions; and ratios of individual ions.

4. A method comprising:
producing a reverse osmosis (RO) permeate blending stream using an RO array of a desalination plant;
producing a nanofiltration (NF) permeate blending stream using an NF array of a desalination plant;
separating fluids produced from one or more production wells that penetrate an oil-bearing layer of a reservoir to produce a produced water (PW) stream;
blending the RO permeate blending stream, the NF permeate blending stream, and the PW stream in a blending system to produce a blended low salinity water stream;
dynamically adjusting operation of the blending system to adjust amounts of the RO permeate blending stream and the NF permeate blending stream to maintain a composition of the blended low salinity water stream within a predetermined operating envelope; and
dynamically adjust amounts of at least one of the RO permeate discharged from the blending system via an RO permeate dump line or the NF permeate discharged from the blending system via an NF permeate dump line.

5. The method of claim 4 , wherein blending comprises blending seawater (SW) with the RO permeate blending stream, the NF permeate blending stream, and the PW stream in the blending system to produce a blended low salinity water stream.

6. The method of claim 4 , wherein dynamically adjusting the operation of the blending system comprises adjusting a valve in the blending system.

7. The method of claim 6 , wherein the valve comprises a valve on the RO permeate dump line.

8. The method of claim 6 , wherein the valve comprises a valve on the NF permeate dump line.

9. The method of claim 6 , wherein the valve comprises a valve on a high salinity water by-pass line that by-passes the desalination plant and feeds seawater (SW) to the blending system.

10. An integrated system comprising:
a control unit;
a plurality of valves controlled by the control unit;
a plurality of flow rate and composition monitors configured to provide measured flow rate data and composition data, respectively, to the control unit;
a reverse osmosis (RO) array configured to produce an RO permeate blending stream;
a nanofiltration (NF) array configured to produce an NF permeate blending stream;
a produced water (PW) stream from a production well; and
a blending system comprising a line configured to blend the RO permeate blending stream, the NF permeate blending stream, and the PW stream into a blended low salinity water stream,
wherein the control unit is configured to:
adjust, in response to the measured flow rate and composition data, at least one of the plurality of valves to maintain a composition of the blended low salinity water stream within a predetermined operating envelope, and
adjust amounts of at least one of the RO permeate discharged from the blending system via an RO permeate dump line or the NF permeate discharged from the blending system via an NF permeate dump line.

11. The integrated system of claim 10 , wherein the flow rate data and composition data pertain to the blended low salinity water stream.

12. The integrated system of claim 10 , further comprising an injection system configured to deliver the blended low salinity water stream to a formation via an injection well.

13. The integrated system of claim 10 , wherein the operating envelope specifies upper and lower limits for a parameter selected from the group consisting of: total dissolved solids (TDS) content; ionic strength; concentrations of individual ions; concentration of types of individual ions; ratios of types of individual ions; and ratios of individual ions.

14. The integrated system of claim 10 , wherein the plurality of valves includes a first valve on an RO permeate dump line and further includes a second valve on an NF permeate dump line.

Assignees

• Bp Exploration Operating Co Ltd

Inventors

• Couves John William
• Crouch John Henry
• Williams John Dale

Classifications

• B01D2313/18

  Specific valves · CPC title

• B01D2317/04

  Elements in parallel · CPC title

• E21B43/20

  Displacing by water · CPC title

• B01D61/027

  Nanofiltration · CPC title

• E21B43/40

  Separation associated with re-injection of separated materials {(E21B43/385 takes precedence)} · CPC title