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EP2149673A1 - Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden - Google Patents

Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden Download PDF

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Publication number
EP2149673A1
EP2149673A1 EP08161579A EP08161579A EP2149673A1 EP 2149673 A1 EP2149673 A1 EP 2149673A1 EP 08161579 A EP08161579 A EP 08161579A EP 08161579 A EP08161579 A EP 08161579A EP 2149673 A1 EP2149673 A1 EP 2149673A1
Authority
EP
European Patent Office
Prior art keywords
pump
liquid
separation vessel
fluid
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP08161579A
Other languages
English (en)
French (fr)
Inventor
Svein Audun Haheim
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to EP08161579A priority Critical patent/EP2149673A1/de
Priority to US13/056,905 priority patent/US20110155385A1/en
Priority to GB1101265A priority patent/GB2475184B/en
Priority to PCT/US2009/052186 priority patent/WO2010014770A1/en
Priority to BRPI0916521A priority patent/BRPI0916521A2/pt
Priority to CN2009801292822A priority patent/CN102105651A/zh
Priority to AU2009276524A priority patent/AU2009276524B2/en
Publication of EP2149673A1 publication Critical patent/EP2149673A1/de
Priority to NO20110309A priority patent/NO20110309A1/no
Withdrawn legal-status Critical Current

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Classifications

    • 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
    • E21B43/34—Arrangements for separating materials produced by the well
    • E21B43/36—Underwater separating arrangements
    • 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
    • E21B43/01—Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells specially adapted for obtaining from underwater installations

Definitions

  • the invention relates to a method and system for subsea processing of multiphase well effluents.
  • a disadvantage of the known subsea processing system is that it comprises a hydraulic pump with a relatively slow response time of at least about twenty seconds and typically about sixty seconds, which hydraulic pump is combined with a differential pressure transducer to control the flowrate of the liquid flowing through the liquid flowline.
  • a further disadvantage of the known subsea processing system is that it will require a low level shutdown system to protect the pump from mechanical damage if the separator is drained. It is an object of the invention to alleviate these disadvantages.
  • a liquid level transmitter measures the liquid level in the separation vessel and transmits the level signal to a controller, which adjusts the pump speed setpoint in a cascade arrangement to maintain the liquid level at a predetermined setpoint.
  • the level controller is tuned to provide extremely fast action for handling level disturbances caused by changes in the liquid feed rate, such that the pump speed setpoint is almost instantly adjusted to respond to changes in liquid level.
  • the level controller also provides stable pump speed when the liquid feed rate is stable.
  • the fast acting variable speed drive receives its speed setpoint from the level controller and increases or decreases the pump speed within 2 seconds, being limited only by the physical capabilities of the particular variable speed drive.
  • This fast acting level controller enables the use of compact separation systems as the liquid interface level can now be maintained within a small boundary.
  • the pump is a gas tolerant or multiphase pump, to ensure occasional separator drainage or gas surge can be tolerated when severe liquid feed disturbances occur which may require a faster pump speed response than is physically possible with the variable speed drive.
  • an inlet of a fluid recirculation conduit may be connected to the liquid enriched fluid transportation conduit at a location downstream of the pump and an outlet of the fluid recirculation conduit is connected to the multiphase well effluent transportation conduit, which conduit is equipped with a valve, which is opened during start up of the pump and which is subsequently closed.
  • a system for subsea processing multiphase well effluents comprising natural gas and liquid from an underwater hydrocarbon containing formation, the system comprising:
  • FIG.1 shows a subsea processing system 1 according to the invention comprising a separation module 2 and a pump module 3 that are retrievably mounted on a base 4, which is mounted on the seabed 5.
  • the separation module 2 comprises a gas-liquid separation vessel 6, which is connected to a multiphase well effluent flowline 7, which is connected via a manifold 8 to a pair of subsea gas wells 9 and 10 which produce a multiphase flow mixture of natural gas, water, condensates and optionally crude oil from an underwater gas reservoir (not shown).
  • the gas-liquid separation vessel 6 is provided with an upper outlet 11 for discharging a gas enriched fluid fraction into a gas transportation conduit 12 and with a lower outlet 13 for discharging a liquid enriched fluid fraction into a liquid transportation conduit 14.
  • the gas and liquid transportation conduits 12 and 14 comprise vertical riser sections 12A, 14A, which are suspended below a floating platform 15, which floats at the water surface 16.
  • the pump module 3 comprises a gas tolerant liquid pump 17, which is driven by an electric motor 18 that is powered via an electrical cable 19 by an electric power source 20 at the platform 15.
  • the electric motor 18 is equipped with a fast acting variable speed drive system, which is coupled, as indicated by dashed line 24, to an assembly of two liquid level transmitters 21 and 22 and a level controller which monitor the liquid level 23 in the separation vessel 6.
  • the level controller provides the speed setpoint to the fast acting variable speed drive system.
  • the level controller will increase the speed of the motor and pump assembly 17,18 within 1 to 2 seconds if the liquid level increases above its setpoint 21 and the level controller will decrease the speed of the motor and pump assembly 17,18 within 1 to 2 seconds if the liquid level 23 drops below the predetermined liquid level controller setpoint 21.
  • a liquid overflow valve 25 is arranged in the gas transportation conduit 12 in the vicinity of the upper gas outlet 11, which valve automatically closes itself if a liquid surge enters the valve.
  • a fraction of the liquid discharged from the lower liquid outlet 13 is circulated back to the multiphase well effluent flowline 7 through a liquid recycling conduit 26, which is equipped with a valve 27, which is opened during the pump start up phase and which is subsequently gradually closed.
  • the valve 27 may comprise a conventional subsea choke and an on-off valve, which does not need to be fast acting as failure to control the recycle flow rate will not have a detrimental effect on the multiphase pump 17.
  • valves 25 and 27 may be simple on off valves, which do not require a complex dynamic control of the valve openings and that the electric motor 18 is the only subsea component which is dynamically controlled by a fast acting variable speed drive system which receives its speed setpoint from a level controller.
  • the modular construction of the system 1 allows replacement, inspection and/or repair of the retrievable pump and separator modules 3 and 2 by disconnecting the stab-in pipe joints 30 and the subsea power cable connector 31 and then lifting the pump and/or separator module 3,2 to a vessel at the water surface 16 for replacement inspection and/or repair.
  • processing system 1 may be installed at the bottom 5 of an ocean, sea, lake and/or river and that the term "subsea" as used in this specification and the accompanying claims should be interpreted extensively so that it embraces all these options.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Geology (AREA)
  • Mining & Mineral Resources (AREA)
  • Physics & Mathematics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Fluid Mechanics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Jet Pumps And Other Pumps (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
EP08161579A 2008-07-31 2008-07-31 Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden Withdrawn EP2149673A1 (de)

Priority Applications (8)

Application Number Priority Date Filing Date Title
EP08161579A EP2149673A1 (de) 2008-07-31 2008-07-31 Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden
US13/056,905 US20110155385A1 (en) 2008-07-31 2009-07-30 Method and system for subsea processing of multiphase well effluents
GB1101265A GB2475184B (en) 2008-07-31 2009-07-30 Method and system for subsea processing of multiphase well effluents
PCT/US2009/052186 WO2010014770A1 (en) 2008-07-31 2009-07-30 Method and system for subsea processing of multiphase well effluents
BRPI0916521A BRPI0916521A2 (pt) 2008-07-31 2009-07-30 método e sistema para processamento submarino de efluentes de poço de multifases
CN2009801292822A CN102105651A (zh) 2008-07-31 2009-07-30 用于多相井流出物的海底处理的方法和系统
AU2009276524A AU2009276524B2 (en) 2008-07-31 2009-07-30 Method and system for subsea processing of multiphase well effluents
NO20110309A NO20110309A1 (no) 2008-07-31 2011-02-25 Fremgangsmate og system for undervannsbehandling av flerfasebronnavlopsvannsportkanaler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP08161579A EP2149673A1 (de) 2008-07-31 2008-07-31 Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden

Publications (1)

Publication Number Publication Date
EP2149673A1 true EP2149673A1 (de) 2010-02-03

Family

ID=40723220

Family Applications (1)

Application Number Title Priority Date Filing Date
EP08161579A Withdrawn EP2149673A1 (de) 2008-07-31 2008-07-31 Verfahren und System zur Unterseeverarbeitung von mehrphasigen Bohrlochfluiden

Country Status (8)

Country Link
US (1) US20110155385A1 (de)
EP (1) EP2149673A1 (de)
CN (1) CN102105651A (de)
AU (1) AU2009276524B2 (de)
BR (1) BRPI0916521A2 (de)
GB (1) GB2475184B (de)
NO (1) NO20110309A1 (de)
WO (1) WO2010014770A1 (de)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2697480A4 (de) * 2011-04-15 2015-10-28 Kongsberg Oil & Gas Technologies As Unterwasserkühlvorrichtung und getrennt aufrufbares tauchpumpenmodul für einen unterwasserwärmetauscher
WO2016075018A1 (en) * 2014-11-10 2016-05-19 Vetco Gray Scandinavia As A multiphase fluid separation and boosting system
CN106401539A (zh) * 2016-10-24 2017-02-15 中海石油(中国)有限公司 具有清管球自动发射功能的水下管汇装置
EP3492694A1 (de) * 2017-12-01 2019-06-05 OneSubsea IP UK Limited Flüssigkeitshalter für ein herstellungssystem
CN110869582A (zh) * 2017-05-03 2020-03-06 巴西石油公司 用于液压驱动的水下泵送的系统和方法

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WO2011137053A1 (en) * 2010-04-27 2011-11-03 Shell Oil Company Method of retrofitting subsea equipment with separation and boosting
IT1401274B1 (it) * 2010-07-30 2013-07-18 Nuova Pignone S R L Macchina sottomarina e metodi per separare componenti di un flusso di materiale
WO2014018585A1 (en) * 2012-07-24 2014-01-30 Shell Oil Company Apparatus, system and method for removing gas from fluid produced from a wellbore
US9551215B2 (en) * 2012-08-13 2017-01-24 Onesubsea Ip Uk Limited Apparatus and system for passively sampling production fluid from a well
SG11201501910TA (en) 2012-09-12 2015-04-29 Fmc Technologies Subsea compressor or pump with hermetically sealed electric motor and with magnetic coupling
WO2014042626A1 (en) 2012-09-12 2014-03-20 Cunningham Christopher E Subsea multiphase pump or compressor with magnetic coupling and cooling or lubrication by liquid or gas extracted from process fluid
AU2012389803B2 (en) 2012-09-12 2017-11-09 Fmc Technologies, Inc. Coupling an electric machine and fluid-end
EP2901017B1 (de) 2012-09-12 2020-06-03 FMC Technologies, Inc. Aufwärtslaufendes flüssigkeitssystem
GB2509165B (en) * 2012-12-21 2018-01-24 Subsea 7 Norway As Subsea processing of well fluids
RU2638492C2 (ru) * 2013-03-15 2017-12-13 ЭфЭмСи ТЕКНОЛОДЖИЗ, ИНК. Подводная скважинная гидравлическая система
KR101507226B1 (ko) 2013-06-05 2015-03-30 현대중공업 주식회사 해저 생산플랜트의 생산성 향상을 위한 듀얼 파이프 시스템
MY173283A (en) 2013-11-07 2020-01-10 Shell Int Research Thermally activated strong acids
CN103883290A (zh) * 2014-03-26 2014-06-25 中国海洋石油总公司 海上油气田多相流混合输送系统
US9133690B1 (en) * 2014-09-09 2015-09-15 Chevron U.S.A. Inc. System and method for mitigating pressure drop at subsea pump startup
EP3054083B1 (de) * 2015-02-05 2017-05-17 Saipem S.p.A. Anlage zur unterwasserverarbeitung von kohlenwasserstoff
EP3569814B1 (de) * 2015-04-01 2022-06-22 Saudi Arabian Oil Company Fluidbetriebenes mischsystem für öl- und gasanwendungen
NO339736B1 (en) * 2015-07-10 2017-01-30 Aker Subsea As Subsea pump and system and methods for control
AU2017415065B2 (en) 2017-05-15 2021-09-16 Aker Solutions As System and method for fluid processing
CN107143321A (zh) * 2017-07-05 2017-09-08 中国石油大学(华东) 一种指状段塞流耗散分离装置
CN107727553B (zh) * 2017-10-31 2023-09-29 中国石油大学(北京) 一种稠油启动压力梯度以及渗流规律测量装置与方法
CN110631870A (zh) * 2018-06-21 2019-12-31 中国石油化工股份有限公司 一种适用海底游离气的取气装置及取气方法
CA3121375A1 (en) * 2018-12-11 2020-06-18 Enpro Subsea Limited Apparatus, systems and methods for oil and gas operations
GB201901257D0 (en) 2019-01-30 2019-03-20 Enpro Subsea Ltd Apparatus, systems and methods for oil and gas operations
CN116087053B (zh) * 2022-12-15 2024-05-07 长江大学 一种研究稠油启动压力梯度对剩余油分布影响的方法

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US3391734A (en) * 1966-01-19 1968-07-09 Mobil Oil Corp Subsea production satellite
US5486106A (en) * 1993-10-18 1996-01-23 Hehl; Karl Hydraulic device for supplying a hydraulic driving unit
EP0833436A2 (de) * 1996-09-27 1998-04-01 General Electric Company Wechselstrommotorregelung für Hochgeschwindigkeits-Tiefbrunnenpumpen
US5865602A (en) * 1995-03-14 1999-02-02 The Boeing Company Aircraft hydraulic pump control system
US7210530B2 (en) 2002-05-02 2007-05-01 Chevron U.S.A. Inc. Subsea separation system

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BR9600249A (pt) * 1996-01-29 1997-12-23 Petroleo Brasileiro Sa Método e aparelhagem para escoamento da produção submarina de petróleo
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NO325930B1 (no) * 2006-07-07 2008-08-18 Shell Int Research Fremgangsmate for a bearbeide og separere en flerfaset bronnstromblanding

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Publication number Priority date Publication date Assignee Title
US3391734A (en) * 1966-01-19 1968-07-09 Mobil Oil Corp Subsea production satellite
US5486106A (en) * 1993-10-18 1996-01-23 Hehl; Karl Hydraulic device for supplying a hydraulic driving unit
US5865602A (en) * 1995-03-14 1999-02-02 The Boeing Company Aircraft hydraulic pump control system
EP0833436A2 (de) * 1996-09-27 1998-04-01 General Electric Company Wechselstrommotorregelung für Hochgeschwindigkeits-Tiefbrunnenpumpen
US7210530B2 (en) 2002-05-02 2007-05-01 Chevron U.S.A. Inc. Subsea separation system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2697480A4 (de) * 2011-04-15 2015-10-28 Kongsberg Oil & Gas Technologies As Unterwasserkühlvorrichtung und getrennt aufrufbares tauchpumpenmodul für einen unterwasserwärmetauscher
WO2016075018A1 (en) * 2014-11-10 2016-05-19 Vetco Gray Scandinavia As A multiphase fluid separation and boosting system
CN106401539A (zh) * 2016-10-24 2017-02-15 中海石油(中国)有限公司 具有清管球自动发射功能的水下管汇装置
CN106401539B (zh) * 2016-10-24 2019-03-01 中海石油(中国)有限公司 具有清管球自动发射功能的水下管汇装置
CN110869582A (zh) * 2017-05-03 2020-03-06 巴西石油公司 用于液压驱动的水下泵送的系统和方法
EP3492694A1 (de) * 2017-12-01 2019-06-05 OneSubsea IP UK Limited Flüssigkeitshalter für ein herstellungssystem
US10844698B2 (en) 2017-12-01 2020-11-24 Onesubsea Ip Uk Limited Liquid retainer for a production system

Also Published As

Publication number Publication date
CN102105651A (zh) 2011-06-22
AU2009276524A1 (en) 2010-02-04
WO2010014770A1 (en) 2010-02-04
AU2009276524B2 (en) 2013-02-28
BRPI0916521A2 (pt) 2015-11-10
NO20110309A1 (no) 2011-04-19
US20110155385A1 (en) 2011-06-30
GB2475184B (en) 2011-10-19
GB201101265D0 (en) 2011-03-09
GB2475184A (en) 2011-05-11

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