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Title:
SYSTEM TO PROVIDE A SUPPLY OF CONTROLLED SALINITY WATER FOR ENHANCED OIL RECOVERY
Document Type and Number:
WIPO Patent Application WO/2013/012548
Kind Code:
A1
Abstract:
A method for providing controlled salinity water for enhanced oil recovery begins by raising the pressure of, and then splitting, a treated seawater feed (11) into two supply streams (21) (41) which are then processed in parallel. One supply stream is passed thorough a nanofiltration membrane system (23) while the other is passed through a reverse osmosis membrane system (43). The permeate streams are then combined for an overall recovery factor in a range of 50% to 65%. The pressure of the first supply stream (21) is preferably reduced prior to treatment, and the nanofiltration membrane system (23) may be housed in a pressure vessel rated for use with a reverse osmosis membrane system (43). Energy can be recovered from the nanofiltration reject stream (27) or the reverse osmosis reject (47) and used to reduce the feed pumping power or provide an inter-stage pressure boost. The single seawater feed allows for a simplified pumping and piping arrangement.

Inventors:
MELLOR GARY HOWARD (GB)
WESTON ROBERT CHARLES WILLIAM (GB)
Application Number:
PCT/US2012/045157
Publication Date:
January 24, 2013
Filing Date:
June 30, 2012
Export Citation:
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Assignee:
CAMERON INT CORP (US)
MELLOR GARY HOWARD (GB)
WESTON ROBERT CHARLES WILLIAM (GB)
International Classes:
B01D61/02; C02F1/44; E21B43/20; C02F103/08
Domestic Patent References:
WO2007138327A12007-12-06
WO2007144591A12007-12-21
Foreign References:
EP1329425A12003-07-23
Other References:
FAKHRU'L-RAZI A ET AL: "Review of technologies for oil and gas produced water treatment", JOURNAL OF HAZARDOUS MATERIALS, ELSEVIER, AMSTERDAM, NL, vol. 170, no. 2-3, 30 October 2009 (2009-10-30), pages 530 - 551, XP026521167, ISSN: 0304-3894, [retrieved on 20090519], DOI: 10.1016/J.JHAZMAT.2009.05.044
Attorney, Agent or Firm:
ROSSLER, Paul E. et al. (100 West 5th Street 10th Floo, Tulsa OK, US)
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Claims:
WHAT IS CLAIMED IS:

1 . A method for providing a supply of controlled salinity water for enhanced oil recovery, the method comprising the steps of:

raising a pressure of a treated seawater feed stream ( 1 1 ), the treated seavvater feed stream having a salinity content above 1 0,000 mg/L;

splitting the raised pressure treated seawater feed stream ( 15) into a first supply stream (21 ) and a second supply stream (41 );

treating in parallel the first and second supply streams (21 )(4 1 ), the first supply stream (2 1 ) being treated by passing it through a nanofiltralion membrane system (23) and the second supply stream (41 ) being treated by passing it through a reverse osmosis membrane system (43); and

blending a nanofiitration permeate stream (25) from the nanofiltralion membrane system (23) with a reverse osmosis permeate stream (45) from the reverse osmosis membrane (43 ) to achieve a mixed supply water stream (61 ) having a salinity in a range of about 4,000 to 10,000 mg/L and a divalent ion concentration less than that of the treated feed water feed stream (1 1 );

the nanofiltralion membrane system (23) and the reverse osmosis membrane system (43) each having about the same recovery factor.

2. A method according to claim 1 wherein the nanofiltralion membrane system (23) is housed in a pressure vessel rated for use with a reverse osmosis membrane system (43 ).

3. A method according to claim 1 wherein the pressure raising step is accomplished using a common feed pressurization system. 4. A method according to claim 1 further comprising the step of reducing a pressure of the first supply stream (21 ) prior to the treating step.

5. A method according to claim 4 wherein the pressure reducing step is accomplished using at least one of a pressure reducing vaive and an energy recovery device.

6. A method according to claim 1 wherein the recovery factor is in a range of 50% to 65%.

7. A method according to claim 1 wherein an overall recovery factor is in a range of 45% to 75%.

8. A method according to claim 7 wherein the overall recovery factor is in a range of 50% to 65%. 9. A method according to claim 1 further comprising the step of recovering energy from at least one of a nanofiJtration reject stream (27) and a reverse osmosis reject stream (47).

10. A method according to claim 9 further comprising the sub-step of using the recovered energy to reduce a feed pumping power. 1 1 . A method according to claim 9 further comprising the sub-step of using the recovered energy to provide an inter-stage pressure boost.

Description:
SYSTEM TO PROVI DE A S UPPLY OF CONTROLLED

SALINITY WATER FOR ENHANCED OI L RECOVERY

BACKGROUND OF THE INVENTION

Enhanced oil recovery from fields can be accomplished by injecting polymer solutions into the oil bearing reservoir. For optimal performance, the polymer solution should use water having a salinity content in a range of about 4,000 to 10,000 mg/L and a low divalent ion (e.g. sulphate, calcium) and hardness content.

Published PCT Application WO 2007/138327 discloses a water treatment system and a method of providing a supply of water of controlled sal inity suitable for injection into an oil bearing reservoir. The system and method includes the steps of: substantial ly desalinating a first feed supply of water to provide a first supply of treated water of low sal inity; treating a second feed supply of water to provide a second supply of treated water having a reduced concentration of divalent ions in comparison to the second feed supply and a higher sal inity than the llrst supply of treated water; and m ixing the first supply of treated water and the second supply of treated water to provide a supply of m ixed water having a desired salinity suitable for injection into an oil bearing reservoir. The first feed supply is preferably treated by reverse osmosis (RO). The second feed supply is preferably treated by nanoflltra ' tion (NF). Publ ished PCT Application WO 2007/ 138327 is herein incorporated by reference in its entirety.

Others have approached the problem of providing water which has the preferred salinity characteristics by first treating seawater with N F and then treating the result ing NF permeate (low sulphate and low hardness water) with RO. For example, Ayirala el al.— in a paper published by the Society of Petroleum Engineers in 201 0, numbered S PE 12996, and titled, "A Designer Water Process for Offshore Low Salinity and Polymer Flooding Appl ications"— disclose a system and method in which filtered seawater llrst passes through two N F stages and the NF permeate then passes through two RO stages. The RO permeate is then blended with the NF reject and RO reject streams. The Ayira!a paper is herein incorporated by reference in its entirety.

A problem with the above serial-type systems and methods is the serial combination limits the overall recovery factor to about 40% to 50% (feed to product). The method also requires separate NF (typically about a 75% recovery factor) and RO (typically about 50% to 65%) systems, each with a dedicated feed pressurizalion system. Additionally, as the produced water flow increases in later field life, the produced water is typically re-injected into the formation after mixing with RO permeate. This makes the requirement for NF redundant while at the same time creating a bottleneck because the RO system lacks sufficient capacity for the new processing demands placed upon it.

Therefore, a need exists to provide a combination of NF and RO membranes which provides the desired salinity level while at the same time increasing the overall recovery factor with reduced equipment space and weight requirements.

SUMMARY OF THE INVENTION

A system and method for providing a supply of controlled sal inity water for enhanced oil recovery includes the steps of:

i. raising a pressure of a treated scawater feed stream having a salinity content above 1 0,000 mg/L;

ii. splitting the raised pressure treated seawater feed stream into a first supply stream and a second supply stream;

iii. treating in parallel the first and second supply streams, the first supply stream being treated by passing it through a nanofl ltration membrane system and the second supply stream being treated by passing it through a reverse osmosis membrane system; and

iv. blending a nanofl ltration permeate stream from the nanofl ltration membrane system with a reverse osmosis permeate stream from the reverse osmosis membrane to achieve a m ixed supply water stream having a sal inity in a range of about 4,000 to 10,000 mg/L and a divalent ion concentration less than that of the treated feed water feed stream.

The overall recovery factor of the above method is in a range of 50% to 65% (and can range between 45% and 75%), with the nanoflltration membrane system and the reverse osmosis membrane system each preferably having about the same recovery factor. The nanofl ltration membrane system may be housed in a pressure vessel rated for use with a reverse osmosis membrane system.

The pressure raising step may be accompl ished using a simplified pumping and piping arrangement because a common feed pressurization system can be employed. The pressure of the first supply stream can then be reduced by way of pressure reducing valves or an energy recovery device prior to ils treating step. Energy can be recovered from a nanofiltration reject stream or a reverse osmosis reject stream (or both streams) and used to reduce the feed pumping power. In applications in which the method employs multiple stages, the recovered energy can be used to provide an inter-stage pressure boost.

Objects of this invention are to provide a system that ( I ) rel ies upon a simpl i fied operating control system, including an on-line conductivity measurement control ; (2) operates the NF and RO systems in parallel, with appropriate NF/RO permeate blending to achieve the desired salinity level; (3) allows the N F membranes to be installed in pressure vessels rated for RO service, thereby permitting change-out of the N F membranes to RO membranes in later Held life; (4) uses a single membrane system in which the NF and RO membranes operate at the same or similar recovery factors; (5) achieves an NF recovery factor in a range of 45% to 85% and a RO recovery factor in a range of 45% to 75% with both recovery factors preferably being about the same or similar in a range of 50% to 65%; (6) accompl ishes a high overall recovery factor (about 45% to 75% with 50% to 65% being typical) while m inimizing weight and space requirements for the pre-treatment system; (7) uses a simplified pumping and piping arrangement because of a common NF/RO feed pressiirization system; and (8) can use energy recovery devices to reduce the feed pressure required for NF operation.

BRIEF DESCRIPTION OF TH E DRAWI NGS

FIG. I is a schematic of a prior art system and method to provide a supply of controlled salinity water for enhanced oil recovery. Pre-treated seawater is split into two streams, with one stream passing through two stages of reverse osmosis (RO) and the other stream, along with an RO reject stream, passing through two stages of nanofiltration (N F). The RO and NF permeate are then blended.

FIG. 2 is a schematic of another prior art system and method to provide a supply of controlled sal inity water for enhanced oil recovery. Pre-treated seawater passes through two NF stages and the NF permeate passes through two RO stages. The RO permeate is then blended with the NF reject and RO reject streams.

FIG. 3 is a schematic of a preferred embodiment of a system and method practiced according to this invention. Pre-treated seawater is split into two streams, with the first stream passing through a single stage of NF and the second streampassing through a single stage of RO. The first stream is preferably at a lower pressure than the second stream. A portion of the N F permeate may be blended with the RO permeate. List of Element Numbers Used in the Drawings

10 Water treatment system 27 NF reject stream

1 1 Treated seawater stream 35 NF permeate stream

13 High-pressure boost pump system 33 Portion of N F permeate production

1 5 Raised pressure feed stream 41 Second supply stream

1 7 Pressure reducing device 43 Reverse osmosis (RO) membrane system

2 1 First supply stream 45 RO permeate stream

23 Nanofiltration (N F) membrane system 47 RO reject stream

25 NF permeate stream 6 1 M ixed water supply DETAI LED DESCRI PTION OF THE PREFERRED EMBODIMENTS

Referring to FIG. 3, a water treatment system 10 for providing a supply of controlled salinity water for enhanced oil recovery operates the nanotl ltration (NF) and reverse osmosis (RO) systems in parallel and relies upon an on-line conductivity measurement control system (A IT) to determine the amount of N F and RO permeate being blended in order to achieve a desired salinity level.

Water treatment system 10 begins with a treated seawater stream 1 1 , which has been pre-treated and filtered by well-known methods to reduce particulate matter, chlorine content, biological activity and scaling. Treated seawater stream 1 1 is routed into a common high-pressure boost pump system 1 3 to create a raised-pressure feed stream 15. The raised pressure feed stream 1 5 is split into two supply streams 2 1 , 4 1 . The first supply stream 2 1 is used to supply a NF membrane system 23. The second supply stream 41 is used to supply a RO membrane system 43.

Un like prior art systems, which rely upon a separate high-pressure booster pump system 1 3 for each supply stream 2 1 , 41 , a common N I7R0 feed pressurization system is employed here. Also, because the pressure required for the NF membrane system 23 is lower than that required for the RO membrane system 43, a pressure reducing device 1 7, such as a pressure reduction valve or an energy recovery system may be employed on the first (NF) supply stream 21 .

Despite the reduced pressure requirements for the NF membrane system 23, and unlike prior art systems, the NF membrane system can be housed in a pressure vessel rated for RO membrane system 43 service. This permits a change-out in later field li fe of the NF membrane system 23 to a supplemental RO membrane system 43. Because the amount of produced water flow increases in later field l ife, the NF membrane system 23 becomes redundant and the RO membrane system 43, if not augmented by an additional RO membrane system, typical ly lacks sufficient capacity for the new processing demands placed upon it. System 10 allows for the NF membrane system 23 to be easily re-deployed and placed into service as additional RO membrane capacity.

The NF membrane system 23 results in a permeate stream 25 and a reject stream 27 which is discharged to waste. Depending on the desired salinity level of the final, mixed water supply 6 1 , a first portion 33 of the NF permeate stream 25 may be mixed with the RO membrane system 43 permeate steam 45. Excess NF permeate production may be recycled upstream of the high-pressure boost pump system 1 3, where the portion 35 is blended with the feed water stream 1 1 .

The RO membrane system 43 system results in a permeate stream 45 and a reject stream 47 which is discharged to waste. The sal inity of the RO permeate stream 45 is extremely low, and in fact is somewhat lower than the optimal range of salinities for oi l recovery applications in which the water is injected into an oil bearing reservoir. The salinity of the NF permeate stream 25 is considerably higher than the salinity of the RO permeate stream 45; however, the concentration of certain, undesirable divalent cations, principally Ca2+, is greatly reduced by the NF membrane system 23. Therefore, a portion 33 of the N F permeate stream 25 is m ixed with the RO permeate stream 45 at a desired m ixing ratio in order to produce a mixed water supply 6 1 which may be injected into an oil bearing reservoir for oil recovery purposes.

The NF membrane system 23 and the RO membrane system 43 each use a single membrane system in which the NF and RO membranes operate at the same or similar recovery factors. The NF membrane system preferably achieves an N F recovery factor in a range of 50% to 65% (but could be in a range of 45% to 85%) and the RO membrane system preferably achieves an RO recovery factor in a range of 50% to 65% (but could be in a range of 45% to 75%). An overall high recovery factor is therefore obtained relative to prior art systems. A further advantage relates to the concentration of divalent ions (e.g. sulfate, calcium, and hardness content) in the mixed water supply 61 . If the concentration of divalent ions in the water supplied to an oil bearing reservoir is above a certain level, then there is a risk that damage may be caused, for example by precipitation of generated surfactants. The reduction in the divalent ion concentration of the NF permeate stream 25 leads to a m ixed water supply 6 1 that has relatively low concentrations of divalent ions.

The m ixing of the NF and RO permeate streams 25, 45, in particular their relative proportions, can be controlled manual ly or automatically using a suitable How control system. Such flow control systems are well known to those skilled in the art. It is particularly preferred that an automatic flow control system is uti l ized that controls the mixing in accordance with a measured variable. For example, conductivity readings of the mixed water supply 61 can be taken as a measure of the total dissolved solids content, and used to control the mixing of the NF and RO permeate streams 25, 45. Suitable control systems, which might incorporate a microprocessor, would readi ly suggest themselves to the skil led reader. The flow rate of the mixed water supply 61 might be controlled in a similar manner. Furthermore, it is possible to make other measurements, such as measurements of calcium ion concentration, and to use these measurements to control the water treatment system 10. It may be necessary to augment these readings with laboratory testing in order to ensure that the system is performing according to expectation. In further embodiments, data relating to in-situ measurements made on the water treatment system 10 are conveyed to a central monitoring location by suitable means, such as by telemetry or over the Internet. While preferred embodiments of a system to provide a supply of controlled salinily water for enhanced oi l recovery have been described with a certain degree of particularity, the following claims define the scope of the invention.