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Patent · US10975677B2 · B2 · US

Pressure exchanger low pressure flow control

(11) Publication number
US10975677B2
(21) Application number
16/346,825
(22) Filing date
2017-11-06
(30) Priority date
2016-11-04
(43) Publication date
2021-04-13
(45) Date of grant
2021-04-13
(51) IPC
E21B 43/26; E21B 43/267; F04F 13/00
(52) CPC
  • E21B Earth or rock drilling; obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells: 43/267, 43/261, 43/40
  • B01D Separation: 21/283, 2313/243
  • F04B Positive-displacement machines for liquids; pumps: 23/06
  • F04F Pumping of fluid by direct contact of another fluid or by using inertia of fluid to be pumped {}; siphons {}: 13/00
(73) Assignee
Schlumberger Technology Corp
(72) Inventors
Rod William Shampine
(54) Title
Pressure exchanger low pressure flow control
(57) Abstract

Apparatus and methods for pressurizing well operations fluids. An example apparatus may include a plurality of pressure exchangers each operable to receive a first fluid via a low-pressure inlet, receive a second fluid via a high-pressure inlet to thereby pressurize and then discharge the first fluid via a high-pressure outlet, and discharge the clean fluid via a low-pressure outlet. The apparatus may further include a fluid control device fluidly connected with the pressure exchangers downstream from the low-pressure outlets. The fluid control device may be a pump operable to draw the clean fluid discharged via the low-pressure outlets and thereby reduce the pressure at the low-pressure outlets and the low-pressure inlets.

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Claims (26)

  1. An apparatus comprising: a fluid pressurizing system comprising: a plurality of pressure exchangers each operable to: receive a first fluid via a low-pressure inlet; receive a second fluid via a high-pressure inlet to pressurize and discharge the first fluid via a high-pressure outlet; and discharge the second fluid via a low-pressure outlet; and a fluid control device fluidly connected with the pressure exchangers downstream from the low-pressure outlets, wherein the fluid control device comprises two or more flow rate control valves connected in parallel along a discharge line, connected in fluid communication with the low-pressure outlets, and collectively operable to control a flow rate of the second fluid while causing a pressure drop that is substantially less than a pressure drop caused by one flow rate control valve.
  2. The apparatus of claim 1 wherein the fluid control device comprises a pump operable to draw the second fluid discharged via the low-pressure outlets and thereby reduce pressure at the low-pressure outlets and the low-pressure inlets.
  3. The apparatus of claim 2 wherein the pump comprises a positive displacement pump.
  4. The apparatus of claim 2 wherein the pump comprises an axial pump or a centrifugal pump.
  5. The apparatus of claim 4 wherein the fluid pressurizing system further comprises the two or more flow rate control valves fluidly connected downstream from the pump.
  6. The apparatus of claim 1 wherein the fluid pressurizing system further comprises a pump fluidly connected downstream from an outlet of a source of the first fluid and upstream from the low-pressure inlets of the pressure exchangers, wherein the pump is operable to decrease pressure at the outlet of the source of the first fluid and increase pressure at the low-pressure inlets and the low-pressure outlets of the pressure exchangers, and wherein the fluid control device comprises a pressure loss device.
  7. The apparatus of claim 6 wherein the pump comprises a positive displacement pump.
  8. The apparatus of claim 6 wherein the pump comprises an axial pump or a centrifugal pump, and wherein the pressure loss device comprises the two or more flow rate control valves.
  9. The apparatus of claim 1 wherein the low-pressure outlets are fluidly connected with a manifold, and wherein the fluid control device is connected to an outlet of the manifold.
  10. The apparatus of claim 1 wherein the first fluid is or comprises a dirty fluid comprising solid particles, wherein the second fluid is or comprises a clean fluid that is substantially free of solid particles, and wherein the fluid pressurizing system comprises a wellsite system operable to inject the dirty fluid into a wellbore during a well treatment operation.
  11. An apparatus comprising: a wellsite system operable to inject a dirty fluid into a wellbore during a well treatment operation, wherein the wellsite system comprises: a first pump operable to pressurize a clean fluid to a high-pressure greater than 5000 psi; a mixer operable at a suction pressure to form a dirty fluid; a plurality of pressure exchangers fluidly connected with the first pump, the mixer, and the wellbore, wherein each pressure exchanger is operable to: receive the dirty fluid from the mixer via a low-pressure inlet; receive the pressurized clean fluid from the first pump via a high-pressure inlet to thereby pressurize and then discharge the received dirty fluid via a high-pressure outlet; and discharge the clean fluid via a low-pressure outlet; and a second pump fluidly connected with the pressure exchangers downstream from the low-pressure outlets, wherein the second pump is operable to draw the clean fluid discharged via the low-pressure outlets and thereby reduce pressure at the low-pressure outlets and the low-pressure inlets, wherein the low-pressure outlets of the pressure exchangers are fluidly connected with a manifold, the second pump is connected to an outlet of the manifold, wherein the second pump is operable to pressurize the discharged clean fluid from the low-pressure outlets to an atmospheric pressure or the suction pressure.
  12. The apparatus of claim 11 wherein the second pump comprises a positive displacement pump.
  13. The apparatus of claim 11 wherein the second pump comprises an axial pump or a centrifugal pump.
  14. The apparatus of claim 13 wherein the wellsite system further comprises a flow rate control valve fluidly connected downstream from the second pump.
  15. The apparatus of claim 11 wherein the wellsite system further comprises a third pump fluidly connected downstream from an outlet of the mixer and upstream from the low-pressure inlets of the pressure exchangers, and wherein the third pump is operable to decrease pressure at the outlet of the mixer.
  16. The apparatus of claim 15 wherein the third pump comprises a positive displacement pump.
  17. The apparatus of claim 15 wherein the third pump comprises an axial pump or a centrifugal pump.
  18. A method comprising: operating a plurality of pressure exchangers by: injecting a first fluid from a source into the pressure exchangers via corresponding low-pressure inlets of the pressure exchangers; injecting a second fluid into the pressure exchangers via corresponding high-pressure inlets of the pressure exchangers to thereby pressurize and then discharge the first fluid via corresponding high-pressure outlets of the pressure exchangers; and discharging the second fluid out of the pressure exchangers via corresponding low-pressure outlets of the pressure exchangers to a manifold comprising an outlet; and operating a pump fluidly connected to the outlet of the manifold to draw the second fluid discharged via the low-pressure outlets and thereby reduce the pressure at the low-pressure outlets and the low-pressure inlets, wherein the pump is operable to direct the discharged second fluid from the manifold to the source or a tank.
  19. The method of claim 18 wherein the pump comprises a positive displacement pump.
  20. The method of claim 18 wherein the pump comprises an axial pump or a centrifugal pump.
  21. The method of claim 20 further comprising controlling flow of the second fluid discharged by the pump via a flow rate control valve connected downstream from the pump to control flow of the first fluid being injected into the pressure exchangers via the corresponding low-pressure inlets.
  22. The method of claim 18 wherein the pump comprises a first pump, and wherein the method further comprises operating a second pump fluidly connected downstream from an outlet of the source of the first fluid and upstream from the low-pressure inlets of the pressure exchangers to decrease pressure at the outlet of the source of the first fluid.
  23. The method of claim 22 wherein the second pump comprises a positive displacement pump.
  24. The method of claim 22 wherein the second pump comprises an axial pump or a centrifugal pump.
  25. The method of claim 18 wherein the first fluid comprises a dirty fluid comprising solid particles, wherein the second fluid is or comprises a clean fluid that is substantially free of solid particles, and wherein the method further comprises injecting the dirty fluid into a wellbore during a well treatment operation.
  26. The method of claim 18, wherein injecting the second fluid into the pressure exchangers thereby pressurizes and then discharges the first fluid at a high pressure greater than 5000 psi from the pressure exchangers.

Description

A variety of fluids are used in oil and gas operations. Fluids may be pumped into the subterranean formation through the use of one or more high-pressure pumps. Dirty fluids, such as solids-laden fluids containing insoluble abrasive solid particles, can reduce functional life and increase maintenance of the high-pressure pumps.

Pressure exchangers utilized in oilfield pumping can create a variety of problems, some of which relate to flow rate and pressure control on the low-pressure side of the pressure exchangers. Pressure exchangers create a relatively high pressure drop, which is at least partially caused by high-pressure fluids (e.g., up to about 20,000 pounds per square inch (PSI)) flowing through relatively constricted pathways at relatively high velocities. On the high-pressure side of the pressure exchangers, such losses are negligible, being on the order of 50 PSI. However, on the low-pressure side, in combination with line friction and pressure drop across a control valve, the pressure drop can exceed the pressure capability of conventional mixers (i.e., blenders). Increasing the output pressure of the mixers increases internal wear rate substantially more than the increase in pressure, leading to frequent equipment failure or repair.

This summary is provided to introduce a selection of concepts that are further described below in the detailed description. This summary is not intended to identify indispensable features of the claimed subject matter, nor is it intended for use as an aid in limiting the scope of the claimed subject matter.

Citations (23)

  • US5935490A
  • US5899272A
  • US20020146325A1
  • US20080087253A1
  • US20100212156A1
  • US20070023718A1
  • US20090180903A1
  • US20110154802A1
  • US20090301725A1
  • WO2010071994A1
  • US20150050167A1
  • US20140048143A1
  • WO2014074939A1
  • US20140128655A1
  • US20160084269A1
  • US20150096739A1
  • US20150184492A1
  • US20160032702A1
  • US20160146229A1
  • US20160160889A1
  • US20160281487A1
  • WO2016176531A1
  • US20170130743A1
Record as JSON
{
  "publication_number": "US10975677B2",
  "country": "US",
  "kind": "B2",
  "title": "Pressure exchanger low pressure flow control",
  "abstract": "Apparatus and methods for pressurizing well operations fluids. An example apparatus may include a plurality of pressure exchangers each operable to receive a first fluid via a low-pressure inlet, receive a second fluid via a high-pressure inlet to thereby pressurize and then discharge the first fluid via a high-pressure outlet, and discharge the clean fluid via a low-pressure outlet. The apparatus may further include a fluid control device fluidly connected with the pressure exchangers downstream from the low-pressure outlets. The fluid control device may be a pump operable to draw the clean fluid discharged via the low-pressure outlets and thereby reduce the pressure at the low-pressure outlets and the low-pressure inlets.",
  "claims": [
    "1. An apparatus comprising: a fluid pressurizing system comprising: a plurality of pressure exchangers each operable to: receive a first fluid via a low-pressure inlet; receive a second fluid via a high-pressure inlet to pressurize and discharge the first fluid via a high-pressure outlet; and discharge the second fluid via a low-pressure outlet; and a fluid control device fluidly connected with the pressure exchangers downstream from the low-pressure outlets, wherein the fluid control device comprises two or more flow rate control valves connected in parallel along a discharge line, connected in fluid communication with the low-pressure outlets, and collectively operable to control a flow rate of the second fluid while causing a pressure drop that is substantially less than a pressure drop caused by one flow rate control valve.",
    "2. The apparatus of claim 1 wherein the fluid control device comprises a pump operable to draw the second fluid discharged via the low-pressure outlets and thereby reduce pressure at the low-pressure outlets and the low-pressure inlets.",
    "3. The apparatus of claim 2 wherein the pump comprises a positive displacement pump.",
    "4. The apparatus of claim 2 wherein the pump comprises an axial pump or a centrifugal pump.",
    "5. The apparatus of claim 4 wherein the fluid pressurizing system further comprises the two or more flow rate control valves fluidly connected downstream from the pump.",
    "6. The apparatus of claim 1 wherein the fluid pressurizing system further comprises a pump fluidly connected downstream from an outlet of a source of the first fluid and upstream from the low-pressure inlets of the pressure exchangers, wherein the pump is operable to decrease pressure at the outlet of the source of the first fluid and increase pressure at the low-pressure inlets and the low-pressure outlets of the pressure exchangers, and wherein the fluid control device comprises a pressure loss device.",
    "7. The apparatus of claim 6 wherein the pump comprises a positive displacement pump.",
    "8. The apparatus of claim 6 wherein the pump comprises an axial pump or a centrifugal pump, and wherein the pressure loss device comprises the two or more flow rate control valves.",
    "9. The apparatus of claim 1 wherein the low-pressure outlets are fluidly connected with a manifold, and wherein the fluid control device is connected to an outlet of the manifold.",
    "10. The apparatus of claim 1 wherein the first fluid is or comprises a dirty fluid comprising solid particles, wherein the second fluid is or comprises a clean fluid that is substantially free of solid particles, and wherein the fluid pressurizing system comprises a wellsite system operable to inject the dirty fluid into a wellbore during a well treatment operation.",
    "11. An apparatus comprising: a wellsite system operable to inject a dirty fluid into a wellbore during a well treatment operation, wherein the wellsite system comprises: a first pump operable to pressurize a clean fluid to a high-pressure greater than 5000 psi; a mixer operable at a suction pressure to form a dirty fluid; a plurality of pressure exchangers fluidly connected with the first pump, the mixer, and the wellbore, wherein each pressure exchanger is operable to: receive the dirty fluid from the mixer via a low-pressure inlet; receive the pressurized clean fluid from the first pump via a high-pressure inlet to thereby pressurize and then discharge the received dirty fluid via a high-pressure outlet; and discharge the clean fluid via a low-pressure outlet; and a second pump fluidly connected with the pressure exchangers downstream from the low-pressure outlets, wherein the second pump is operable to draw the clean fluid discharged via the low-pressure outlets and thereby reduce pressure at the low-pressure outlets and the low-pressure inlets, wherein the low-pressure outlets of the pressure exchangers are fluidly connected with a manifold, the second pump is connected to an outlet of the manifold, wherein the second pump is operable to pressurize the discharged clean fluid from the low-pressure outlets to an atmospheric pressure or the suction pressure.",
    "12. The apparatus of claim 11 wherein the second pump comprises a positive displacement pump.",
    "13. The apparatus of claim 11 wherein the second pump comprises an axial pump or a centrifugal pump.",
    "14. The apparatus of claim 13 wherein the wellsite system further comprises a flow rate control valve fluidly connected downstream from the second pump.",
    "15. The apparatus of claim 11 wherein the wellsite system further comprises a third pump fluidly connected downstream from an outlet of the mixer and upstream from the low-pressure inlets of the pressure exchangers, and wherein the third pump is operable to decrease pressure at the outlet of the mixer.",
    "16. The apparatus of claim 15 wherein the third pump comprises a positive displacement pump.",
    "17. The apparatus of claim 15 wherein the third pump comprises an axial pump or a centrifugal pump.",
    "18. A method comprising: operating a plurality of pressure exchangers by: injecting a first fluid from a source into the pressure exchangers via corresponding low-pressure inlets of the pressure exchangers; injecting a second fluid into the pressure exchangers via corresponding high-pressure inlets of the pressure exchangers to thereby pressurize and then discharge the first fluid via corresponding high-pressure outlets of the pressure exchangers; and discharging the second fluid out of the pressure exchangers via corresponding low-pressure outlets of the pressure exchangers to a manifold comprising an outlet; and operating a pump fluidly connected to the outlet of the manifold to draw the second fluid discharged via the low-pressure outlets and thereby reduce the pressure at the low-pressure outlets and the low-pressure inlets, wherein the pump is operable to direct the discharged second fluid from the manifold to the source or a tank.",
    "19. The method of claim 18 wherein the pump comprises a positive displacement pump.",
    "20. The method of claim 18 wherein the pump comprises an axial pump or a centrifugal pump.",
    "21. The method of claim 20 further comprising controlling flow of the second fluid discharged by the pump via a flow rate control valve connected downstream from the pump to control flow of the first fluid being injected into the pressure exchangers via the corresponding low-pressure inlets.",
    "22. The method of claim 18 wherein the pump comprises a first pump, and wherein the method further comprises operating a second pump fluidly connected downstream from an outlet of the source of the first fluid and upstream from the low-pressure inlets of the pressure exchangers to decrease pressure at the outlet of the source of the first fluid.",
    "23. The method of claim 22 wherein the second pump comprises a positive displacement pump.",
    "24. The method of claim 22 wherein the second pump comprises an axial pump or a centrifugal pump.",
    "25. The method of claim 18 wherein the first fluid comprises a dirty fluid comprising solid particles, wherein the second fluid is or comprises a clean fluid that is substantially free of solid particles, and wherein the method further comprises injecting the dirty fluid into a wellbore during a well treatment operation.",
    "26. The method of claim 18, wherein injecting the second fluid into the pressure exchangers thereby pressurizes and then discharges the first fluid at a high pressure greater than 5000 psi from the pressure exchangers."
  ],
  "description_excerpt": "A variety of fluids are used in oil and gas operations. Fluids may be pumped into the subterranean formation through the use of one or more high-pressure pumps. Dirty fluids, such as solids-laden fluids containing insoluble abrasive solid particles, can reduce functional life and increase maintenance of the high-pressure pumps.\n\nPressure exchangers utilized in oilfield pumping can create a variety of problems, some of which relate to flow rate and pressure control on the low-pressure side of the pressure exchangers. Pressure exchangers create a relatively high pressure drop, which is at least partially caused by high-pressure fluids (e.g., up to about 20,000 pounds per square inch (PSI)) flowing through relatively constricted pathways at relatively high velocities. On the high-pressure side of the pressure exchangers, such losses are negligible, being on the order of 50 PSI. However, on the low-pressure side, in combination with line friction and pressure drop across a control valve, the pressure drop can exceed the pressure capability of conventional mixers (i.e., blenders). Increasing the output pressure of the mixers increases internal wear rate substantially more than the increase in pressure, leading to frequent equipment failure or repair.\n\nThis summary is provided to introduce a selection of concepts that are further described below in the detailed description. This summary is not intended to identify indispensable features of the claimed subject matter, nor is it intended for use as an aid in limiting the scope of the claimed subject matter.",
  "cpc": [
    "E21B 43/267",
    "B01D 21/283",
    "B01D 2313/243",
    "E21B 43/261",
    "E21B 43/40",
    "F04B 23/06",
    "F04F 13/00"
  ],
  "ipc": [
    "E21B 43/26",
    "E21B 43/267",
    "F04F 13/00"
  ],
  "assignees": [
    "Schlumberger Technology Corp"
  ],
  "inventors": [
    "Rod William Shampine"
  ],
  "filing_date": "2017-11-06",
  "publication_date": "2021-04-13",
  "grant_date": "2021-04-13",
  "priority_date": "2016-11-04",
  "application_number": "US-201716346825-A",
  "family_id": "62076399",
  "cited_by_count": 8,
  "citations": [
    "US5935490A",
    "US5899272A",
    "US20020146325A1",
    "US20080087253A1",
    "US20100212156A1",
    "US20070023718A1",
    "US20090180903A1",
    "US20110154802A1",
    "US20090301725A1",
    "WO2010071994A1",
    "US20150050167A1",
    "US20140048143A1",
    "WO2014074939A1",
    "US20140128655A1",
    "US20160084269A1",
    "US20150096739A1",
    "US20150184492A1",
    "US20160032702A1",
    "US20160146229A1",
    "US20160160889A1",
    "US20160281487A1",
    "WO2016176531A1",
    "US20170130743A1"
  ]
}

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