WO2016176531A1 - Fracturation à l'aide d'un échangeur de pression optimisé - Google Patents
Fracturation à l'aide d'un échangeur de pression optimisé Download PDFInfo
- Publication number
- WO2016176531A1 WO2016176531A1 PCT/US2016/029961 US2016029961W WO2016176531A1 WO 2016176531 A1 WO2016176531 A1 WO 2016176531A1 US 2016029961 W US2016029961 W US 2016029961W WO 2016176531 A1 WO2016176531 A1 WO 2016176531A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fluid
- dirty
- pressure
- clean
- stream
- Prior art date
Links
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Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04F—PUMPING OF FLUID BY DIRECT CONTACT OF ANOTHER FLUID OR BY USING INERTIA OF FLUID TO BE PUMPED; SIPHONS
- F04F13/00—Pressure exchangers
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B43/00—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
- E21B43/25—Methods for stimulating production
- E21B43/26—Methods for stimulating production by forming crevices or fractures
- E21B43/2607—Surface equipment specially adapted for fracturing operations
Definitions
- the present disclosure also introduces a method that includes forming a stream of dirty fluid at a first pressure and forming a stream of clean fluid at a second pressure, the second pressure being substantially greater than the first pressure.
- the method also includes
- FIG. 5 according to one or more aspects of the present disclosure.
- the clean fluid 120 may be a combustible or cryogenic gas that, upon combustion or heating, acts to pressurize the dirty fluid 110, whether instead of or in addition to the higher pressure of the clean fluid 120 acting to pressurize the dirty fluid 110.
- the boundary 103 and/or other components may include one or more burst discs to protect against overpressure from the clean fluid 120.
- the boundary 103 may continue to reduce the first volume 104 as the pressurized dirty fluid 110 is conducted from the chamber 100 to a wellhead (not shown) at a higher pressure than when the dirty fluid 110 entered the chamber 100, such as via a first outlet valve 112 and one or more conduits 113.
- the second inlet valve 107 may then be closed, for example, in response to pressure sensed by a pressure transducer within the chamber 100 and/or along one or more of the conduits and/or inlet valves.
- the inlets and outlets 204-207 may also be configured to permit fluid flow into and out of more than one chamber 150 at a time.
- the non-pressurized dirty fluid inlet 204 may be sized to simultaneously fill more than one chamber 150
- the inlet and outlets 204- 207 may be configured to permit non-pressurized dirty fluid to be conducted into a chamber 150 while the reduced-pressure clean fluid is simultaneously being discharged from that chamber 150.
- the fluid flow through the spaces 261, 262, 263 within the pressure exchanger 200 may form a fluid film or layer operating as a hydraulic bearing or otherwise providing lubrication between the rotating rotor 201 and the static housing assembly, such as may prevent or reduce contact or friction between the rotor 201 and the housing assembly during pressurizing operations.
- the flow of fluids through the spaces 261, 262, 263 may be biased such that substantially just the clean fluid, and not the dirty fluid, flows through the spaces 261, 262, 263 during pressurizing operations, as indicated by arrows 265, 266, 267. Biasing the flow of clean fluid through the spaces 261, 262, 263 may also cause the clean/dirty fluid boundary 103 (shown in FIGS. 1-4) to maintain a net velocity directed toward the dirty fluid outlet 205. Accordingly, biasing the flow of clean fluid may result in substantially just the clean fluid being
- the portion of the fluid flowing through the spaces 261, 262, 263 includes the difference between the received and discharged clean fluid flows forced to flow through the spaces 261, 262, 263 toward the dirty fluid inlet and outlet 331, 333 and merge with or flow into the dirty fluid stream.
- the clean fluid flowing through the spaces 261, 262, 263 may merge with or flow into the stream of dirty fluid being received via the dirty fluid inlet 331 at the interface of the dirty fluid inlet 331 and the chamber 250 and/or the clean fluid flowing through the spaces 261, 262, 263 may merge with or flow into the stream of dirty fluid being discharged via the dirty fluid outlet 333 at the interface of the dirty fluid outlet 333 and the chamber 250.
- Each fluid control valve 323, 326-329, 335-338, 367, 369 may be actuated remotely by a corresponding actuator (not shown) coupled with each fluid control valve 323, 326-329, 335-338, 367, 369.
- the actuators may be or comprise electric actuators, such as solenoids or motors, or fluid actuators, such as pneumatic or hydraulic cylinders or rotary actuators.
- the fluid control valves 323, 326-329, 335-338, 367, 369 may also be actuated manually, such as by a lever (not shown).
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Environmental & Geological Engineering (AREA)
- Fluid Mechanics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Details And Applications Of Rotary Liquid Pumps (AREA)
Abstract
L'invention porte sur un appareil et des procédés pour la formation et la mise sous pression de fluides pour des opérations dans des puits, utilisant un flux de fluide sale à une première pression et un flux de fluide propre à une seconde pression qui est sensiblement supérieure à la première pression. Un échangeur de pression reçoit les flux de fluides propre et sale pour mettre sous pression le flux de fluide sale. Une partie du fluide propre est envoyée dans le fluide sale à l'intérieur de l'échangeur de pression. Un flux du fluide sale sous pression est amené à sortir de l'échangeur de pression, ainsi qu'un autre flux comprenant du fluide propre et peut-être sale.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201562155077P | 2015-04-30 | 2015-04-30 | |
US62/155,077 | 2015-04-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2016176531A1 true WO2016176531A1 (fr) | 2016-11-03 |
Family
ID=57198811
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2016/029961 WO2016176531A1 (fr) | 2015-04-30 | 2016-04-29 | Fracturation à l'aide d'un échangeur de pression optimisé |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2016176531A1 (fr) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2018085745A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Prévention de l'usure d'un échangeur de pression |
WO2018085741A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Source d'oscillation de pression d'échangeur de pression |
WO2018085746A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Commande d'écoulement basse pression d'échangeur de pression |
WO2018085743A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Opérations de flux divisé avec échangeurs de pression |
WO2018085740A3 (fr) * | 2016-11-04 | 2018-07-26 | Schlumberger Technology Corporation | Échangeur de pression à rapport de pression |
US10385841B2 (en) | 2017-02-09 | 2019-08-20 | Caterpillar Inc. | Pump monitoring and notification system |
US10844854B2 (en) | 2017-01-23 | 2020-11-24 | Caterpillar Inc. | Pump failure differentiation system |
US11157025B2 (en) | 2016-11-04 | 2021-10-26 | Schlumberger Technology Corporation | Pressure exchanger manifold resonance reduction |
CN114251079A (zh) * | 2021-12-15 | 2022-03-29 | 中国地质大学(北京) | 一种煤层气开采用高效压裂设备 |
WO2023283454A3 (fr) * | 2021-07-09 | 2024-04-04 | Energy Recovery, Inc. | Commande d'un système d'échangeur de pression |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH062778A (ja) * | 1992-06-19 | 1994-01-11 | Osaka Gas Co Ltd | 高温気体用の四方弁 |
US5899272A (en) * | 1997-05-21 | 1999-05-04 | Foremost Industries Inc. | Fracture treatment system for wells |
US20060065400A1 (en) * | 2004-09-30 | 2006-03-30 | Smith David R | Method and apparatus for stimulating a subterranean formation using liquefied natural gas |
US20090205869A1 (en) * | 2008-02-15 | 2009-08-20 | National Oilwell Varco, .Lp. | Method and system of monitoring rotational time of rotatable equipment |
US20140076577A1 (en) * | 2011-03-29 | 2014-03-20 | Schlumberger Technology Corporation | System and method for reducing pressure fluctuations in an oilfield pumping system |
-
2016
- 2016-04-29 WO PCT/US2016/029961 patent/WO2016176531A1/fr active Application Filing
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH062778A (ja) * | 1992-06-19 | 1994-01-11 | Osaka Gas Co Ltd | 高温気体用の四方弁 |
US5899272A (en) * | 1997-05-21 | 1999-05-04 | Foremost Industries Inc. | Fracture treatment system for wells |
US20060065400A1 (en) * | 2004-09-30 | 2006-03-30 | Smith David R | Method and apparatus for stimulating a subterranean formation using liquefied natural gas |
US20090205869A1 (en) * | 2008-02-15 | 2009-08-20 | National Oilwell Varco, .Lp. | Method and system of monitoring rotational time of rotatable equipment |
US20140076577A1 (en) * | 2011-03-29 | 2014-03-20 | Schlumberger Technology Corporation | System and method for reducing pressure fluctuations in an oilfield pumping system |
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10975677B2 (en) | 2016-11-04 | 2021-04-13 | Schlumberger Technology Corporation | Pressure exchanger low pressure flow control |
US11346372B2 (en) | 2016-11-04 | 2022-05-31 | Schlumberger Technology Corporation | Split stream operations with pressure exchangers |
WO2018085745A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Prévention de l'usure d'un échangeur de pression |
WO2018085743A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Opérations de flux divisé avec échangeurs de pression |
US10995774B2 (en) | 2016-11-04 | 2021-05-04 | Schlumberger Technology Corporation | Pressure exchanger with pressure ratio |
WO2018085741A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Source d'oscillation de pression d'échangeur de pression |
US11157025B2 (en) | 2016-11-04 | 2021-10-26 | Schlumberger Technology Corporation | Pressure exchanger manifold resonance reduction |
WO2018085746A1 (fr) * | 2016-11-04 | 2018-05-11 | Schlumberger Technology Corporation | Commande d'écoulement basse pression d'échangeur de pression |
WO2018085740A3 (fr) * | 2016-11-04 | 2018-07-26 | Schlumberger Technology Corporation | Échangeur de pression à rapport de pression |
US10961823B2 (en) | 2016-11-04 | 2021-03-30 | Schlumberger Technology Corporation | Pressure exchanger pressure oscillation source |
US11460051B2 (en) | 2016-11-04 | 2022-10-04 | Schlumberger Technology Corporation | Pressure exchanger wear prevention |
US10844854B2 (en) | 2017-01-23 | 2020-11-24 | Caterpillar Inc. | Pump failure differentiation system |
US10385841B2 (en) | 2017-02-09 | 2019-08-20 | Caterpillar Inc. | Pump monitoring and notification system |
WO2023283454A3 (fr) * | 2021-07-09 | 2024-04-04 | Energy Recovery, Inc. | Commande d'un système d'échangeur de pression |
US11959502B2 (en) | 2021-07-09 | 2024-04-16 | Energy Recovery, Inc | Control of a pressure exchanger system |
CN114251079B (zh) * | 2021-12-15 | 2022-09-23 | 中国地质大学(北京) | 一种煤层气开采用高效压裂设备 |
CN114251079A (zh) * | 2021-12-15 | 2022-03-29 | 中国地质大学(北京) | 一种煤层气开采用高效压裂设备 |
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