AR034443A1 - Un procedimiento de transporte de gas humedo a traves de una tuberia submarina. - Google Patents

Un procedimiento de transporte de gas humedo a traves de una tuberia submarina.

Info

Publication number
AR034443A1
AR034443A1 ARP020102162A ARP020102162A AR034443A1 AR 034443 A1 AR034443 A1 AR 034443A1 AR P020102162 A ARP020102162 A AR P020102162A AR P020102162 A ARP020102162 A AR P020102162A AR 034443 A1 AR034443 A1 AR 034443A1
Authority
AR
Argentina
Prior art keywords
heat transfer
hydrocarbon stream
conducted
liquid phase
transfer medium
Prior art date
Application number
ARP020102162A
Other languages
English (en)
Inventor
John J Waycuilis
Stephen D York
Original Assignee
Marathon Oil Co
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 Marathon Oil Co filed Critical Marathon Oil Co
Publication of AR034443A1 publication Critical patent/AR034443A1/es

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C11/00—Use of gas-solvents or gas-sorbents in vessels
    • F17C11/007—Use of gas-solvents or gas-sorbents in vessels for hydrocarbon gases, such as methane or natural gas, propane, butane or mixtures thereof [LPG]
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D13/00—Heat-exchange apparatus using a fluidised bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00115—Controlling the temperature by indirect heat exchange with heat exchange elements inside the bed of solid particles
    • B01J2208/0015—Plates; Cylinders

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

Un procedimiento de transporte para un gas húmedo emplea un intercambiador de calor submarino que tiene una primera y una segunda trayectoria de flujo separadas por una superficie de transferencia de calor. Se conduce un medio de transferencia de calor más frío a través de la primera trayectoria de flujo en una fase líquida mientras que una corriente de hidrocarburos más tibia que tiene una fase gaseosa de hidrocarburos y una fase líquida acuosa es conducida a través de la segunda trayectoria de flujo que enfría la corriente de hidrocarburos y calienta el medio de transferencia de calor. El medio de transferencia de calor es convertido por calentamiento en una fase de vapor que es conducida hacia un condensador pasivo asociado con el cambiador de calor submarino. La temperatura ambiente del agua marina que sumerge el condensador enfría el medio de transferencia de calor y lo retorna a la fase líquida para su uso repetido en el intercambiador de calor. Una porción de la corriente de hidrocarburos es convertida por enfriamiento en una pluralidad de partículas de hidrato de gas sólido, mientras que un medio de partículas sólidas transportado dentro de la corriente de hidrocarburos previene la formación de partículas de hidrato de gas en la segunda trayectoria de flujo. Las partículas del hidrato de gas se mezclan con los componentes remanentes de la fase líquida de la corriente de hidrocarburos para formar una suspensión de hidrato de gas que es retirada de la segunda trayectoria de flujo y conducida a través de una tubería submarina de transporte.
ARP020102162A 2001-06-08 2002-06-07 Un procedimiento de transporte de gas humedo a traves de una tuberia submarina. AR034443A1 (es)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US09/877,798 US6703534B2 (en) 1999-12-30 2001-06-08 Transport of a wet gas through a subsea pipeline

Publications (1)

Publication Number Publication Date
AR034443A1 true AR034443A1 (es) 2004-02-25

Family

ID=25370750

Family Applications (1)

Application Number Title Priority Date Filing Date
ARP020102162A AR034443A1 (es) 2001-06-08 2002-06-07 Un procedimiento de transporte de gas humedo a traves de una tuberia submarina.

Country Status (8)

Country Link
US (1) US6703534B2 (es)
AR (1) AR034443A1 (es)
AU (1) AU2002312313A1 (es)
BR (1) BR0210271A (es)
NO (1) NO20035417D0 (es)
OA (1) OA12616A (es)
RU (1) RU2003135423A (es)
WO (1) WO2002101277A2 (es)

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NO985001D0 (no) * 1998-10-27 1998-10-27 Eriksson Nyfotek As Leiv FremgangsmÕte og system for transport av en str°m av fluide hydrokarboner inneholdende vann
WO2001038811A1 (fr) 1999-11-26 2001-05-31 Nkk Corporation Materiau de stockage thermique utilisant un dispositif de stockage hydrate et thermique et procede de production de ce materiau
US7511180B2 (en) * 1999-12-30 2009-03-31 Marathon Oil Company Stabilizing petroleum liquids for storage or transport
US20080072495A1 (en) * 1999-12-30 2008-03-27 Waycuilis John J Hydrate formation for gas separation or transport
US8161998B2 (en) 2007-06-04 2012-04-24 Matos Jeffrey A Frozen/chilled fluid for pipelines and for storage facilities
US7008544B2 (en) * 2002-05-08 2006-03-07 Marine Desalination Systems, L.L.C. Hydrate-based desalination/purification using permeable support member
EP1510763B1 (en) * 2002-05-31 2012-02-01 JFE Engineering Corporation Apparatus for producing hydrate slurry
WO2005005567A1 (en) * 2003-07-02 2005-01-20 Exxonmobil Upstream Research Company A method for inhibiting hydrate formation
US20050137432A1 (en) 2003-12-17 2005-06-23 Chevron U.S.A. Inc. Method and system for preventing clathrate hydrate blockage formation in flow lines by enhancing water cut
EA009751B1 (ru) * 2004-07-29 2008-04-28 Твистер Б.В. Теплообменный аппарат со средствами рециркуляции очищающих частиц
GB0424387D0 (en) * 2004-11-04 2004-12-08 Univ Heriot Watt Novel hydrate based systems
CA2630998C (en) 2005-12-06 2014-01-21 Bp Exploration Operating Company Limited Process for regasifying a gas hydrate slurry
RU2425860C2 (ru) * 2006-03-15 2011-08-10 Эксонмобил Апстрим Рисерч Компани Способ получения не образующей пробки суспензии гидрата
US7958939B2 (en) * 2006-03-24 2011-06-14 Exxonmobil Upstream Research Co. Composition and method for producing a pumpable hydrocarbon hydrate slurry at high water-cut
NO326573B1 (no) * 2007-03-21 2009-01-12 Sinvent As Fremgangsmate og anordning for forbehandling av en strom av fluide hydrokarboner inneholdende vann.
NO330761B1 (no) * 2007-06-01 2011-07-04 Fmc Kongsberg Subsea As Undersjoisk kjoleenhet og fremgangsmate for undersjoisk kjoling
WO2009042319A1 (en) * 2007-09-25 2009-04-02 Exxonmobil Upstream Research Company Method for managing hydrates in subsea production line
US8469101B2 (en) 2007-09-25 2013-06-25 Exxonmobil Upstream Research Company Method and apparatus for flow assurance management in subsea single production flowline
EP2196521A4 (en) * 2007-10-03 2014-08-20 Mitsui Shipbuilding Eng DEVICE FOR PRODUCING GAS HYDRATES
WO2010009110A2 (en) * 2008-07-17 2010-01-21 Vetco Gray Scandinavia.As System and method for sub-cooling hydrocarbon production fluid for transport
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US20120322693A1 (en) 2010-03-05 2012-12-20 Lachance Jason W System and method for creating flowable hydrate slurries in production fluids
US9068451B2 (en) * 2010-03-11 2015-06-30 Sinvent As Treatment of produced hydrocarbon fluid containing water
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US8978769B2 (en) * 2011-05-12 2015-03-17 Richard John Moore Offshore hydrocarbon cooling system
CA2840701C (en) * 2011-07-01 2019-07-30 Statoil Petroleum As Subsea heat exchanger and method for temperature control
US10590742B2 (en) * 2011-07-15 2020-03-17 Exxonmobil Upstream Research Company Protecting a fluid stream from fouling using a phase change material
US9303819B2 (en) 2012-06-04 2016-04-05 Elwha Llc Fluid recovery in chilled clathrate transportation systems
US9822932B2 (en) 2012-06-04 2017-11-21 Elwha Llc Chilled clathrate transportation system
RU2505742C1 (ru) * 2012-08-16 2014-01-27 Виктор Дорофеевич Лапшин Устройство для доставки природного газа
RU2504712C1 (ru) * 2012-08-16 2014-01-20 Виктор Дорофеевич Лапшин Способ доставки природного газа
WO2016054695A1 (en) * 2014-10-09 2016-04-14 Subcool Technologies Pty Ltd System and method for subsea cooling a wellhead gas to produce a single phase dew-pointed gas
WO2016064480A1 (en) * 2014-10-22 2016-04-28 Exxonmobil Upstream Research Company Entraining hydrate particles in a gas stream
WO2016195842A1 (en) * 2015-06-04 2016-12-08 Exxonmobil Upstream Research Company System and process for managing hydrate and wax deposition in hydrocarbon pipelines
US10233738B2 (en) 2015-08-06 2019-03-19 Subcool Technologies Pty Ltd. System and method for processing natural gas produced from a subsea well
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Also Published As

Publication number Publication date
WO2002101277A2 (en) 2002-12-19
NO20035417D0 (no) 2003-12-05
WO2002101277A3 (en) 2003-03-13
AU2002312313A1 (en) 2002-12-23
RU2003135423A (ru) 2005-05-10
US20020120172A1 (en) 2002-08-29
BR0210271A (pt) 2004-07-20
OA12616A (en) 2006-06-12
US6703534B2 (en) 2004-03-09

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