WO2003066423A1 - Cuve destinee au transport de lpg et de co2 liquide et systeme de production d'energie sans emission de co2 dans l'atmosphere - Google Patents

Cuve destinee au transport de lpg et de co2 liquide et systeme de production d'energie sans emission de co2 dans l'atmosphere Download PDF

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Publication number
WO2003066423A1
WO2003066423A1 PCT/NO2002/000442 NO0200442W WO03066423A1 WO 2003066423 A1 WO2003066423 A1 WO 2003066423A1 NO 0200442 W NO0200442 W NO 0200442W WO 03066423 A1 WO03066423 A1 WO 03066423A1
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WO
WIPO (PCT)
Prior art keywords
vessel
liquid
tanks
equipment
condensate
Prior art date
Application number
PCT/NO2002/000442
Other languages
English (en)
Inventor
Svein Inge Eide
Kåre G. Breivik
Original Assignee
Statoil Asa
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 Statoil Asa filed Critical Statoil Asa
Priority to AU2002367607A priority Critical patent/AU2002367607A1/en
Publication of WO2003066423A1 publication Critical patent/WO2003066423A1/fr

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/0605—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the feed stream
    • F25J3/061—Natural gas or substitute natural gas
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B25/00—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby
    • B63B25/02—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods
    • B63B25/08—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid
    • B63B25/12—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid closed
    • B63B25/16—Load-accommodating arrangements, e.g. stowing, trimming; Vessels characterised thereby for bulk goods fluid closed heat-insulated
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63B—SHIPS OR OTHER WATERBORNE VESSELS; EQUIPMENT FOR SHIPPING 
    • B63B35/00—Vessels or similar floating structures specially adapted for specific purposes and not otherwise provided for
    • B63B35/44—Floating buildings, stores, drilling platforms, or workshops, e.g. carrying water-oil separating devices
    • 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
    • F17C1/00—Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
    • F17C1/002—Storage in barges or on ships
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/0635—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of CnHm with 1 carbon atom or more
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/06—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation
    • F25J3/063—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream
    • F25J3/0645—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by partial condensation characterised by the separated product stream separation of CnHm with 3 carbon atoms or more
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/03—Orientation
    • F17C2201/032—Orientation with substantially vertical main axis
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/05—Size
    • F17C2201/052—Size large (>1000 m3)
    • 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/05—Size
    • F17C2201/054—Size medium (>1 m3)
    • 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
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/03—Thermal insulations
    • 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
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602—Wall structures; Special features thereof
    • F17C2203/0612—Wall structures
    • F17C2203/0614—Single wall
    • F17C2203/0619—Single wall with two layers
    • 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
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0634—Materials for walls or layers thereof
    • F17C2203/0636—Metals
    • F17C2203/0639—Steels
    • F17C2203/0643—Stainless steels
    • 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
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/01—Mounting arrangements
    • F17C2205/0123—Mounting arrangements characterised by number of vessels
    • F17C2205/013—Two or more vessels
    • 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
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/01—Mounting arrangements
    • F17C2205/0123—Mounting arrangements characterised by number of vessels
    • F17C2205/013—Two or more vessels
    • F17C2205/0134—Two or more vessels characterised by the presence of fluid connection between vessels
    • 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
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/013—Carbone dioxide
    • 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • 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
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • F17C2221/035—Propane butane, e.g. LPG, GPL
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0107—Single phase
    • F17C2223/0123—Single phase gaseous, e.g. CNG, GNC
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied gas
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/035—High pressure (>10 bar)
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/036—Very high pressure (>80 bar)
    • 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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • 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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0171—Arrangement
    • F17C2227/0178—Arrangement in the vessel
    • 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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0337—Heat exchange with the fluid by cooling
    • 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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0367—Localisation of heat exchange
    • F17C2227/0369—Localisation of heat exchange in or on a vessel
    • F17C2227/0376—Localisation of heat exchange in or on a vessel in wall contact
    • F17C2227/0383—Localisation of heat exchange in or on a vessel in wall contact outside the vessel
    • F17C2227/0386—Localisation of heat exchange in or on a vessel in wall contact outside the vessel with a jacket
    • 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
    • F17C2260/00—Purposes of gas storage and gas handling
    • F17C2260/03—Dealing with losses
    • F17C2260/031—Dealing with losses due to heat transfer
    • F17C2260/032—Avoiding freezing or defrosting
    • 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
    • F17C2260/00—Purposes of gas storage and gas handling
    • F17C2260/04—Reducing risks and environmental impact
    • F17C2260/044—Avoiding pollution or contamination
    • 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/01—Purifying the fluid
    • F17C2265/015—Purifying the fluid by separating
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0102—Applications for fluid transport or storage on or in the water
    • F17C2270/0105—Ships
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0102—Applications for fluid transport or storage on or in the water
    • F17C2270/0118—Offshore
    • F17C2270/0121—Platforms
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0134—Applications for fluid transport or storage placed above the ground
    • F17C2270/0136—Terminals
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0142—Applications for fluid transport or storage placed underground
    • F17C2270/0144—Type of cavity
    • F17C2270/0155—Type of cavity by using natural cavities
    • 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
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0142—Applications for fluid transport or storage placed underground
    • F17C2270/0157—Location of cavity
    • F17C2270/0163—Location of cavity offshore
    • 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
    • F17C2270/00—Applications
    • F17C2270/05—Applications for industrial use
    • F17C2270/0581—Power plants
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2210/00—Processes characterised by the type or other details of the feed stream
    • F25J2210/80—Carbon dioxide
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2270/00—Refrigeration techniques used
    • F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
    • F25J2270/904—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration by liquid or gaseous cryogen in an open loop
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/70—Processing device is mobile or transportable, e.g. by hand, car, ship, rocket engine etc.
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00—Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/72—Processing device is used off-shore, e.g. on a platform or floating on a ship or barge
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
    • Y02C20/00—Capture or disposal of greenhouse gases
    • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Definitions

  • the present invention regards a vessel equipped for loading, transport and unloading of LPG, condensate or another liquid that is stable under atmospheric pressure, and liquid CO 2 , which vessel further is comprising a separation unit capable to receive an inflow for subsequent separation to components for storage in the vessel or supply to another unit.
  • the present invention also regards a vessel equipped for loading, transport and unloading of the above mentioned types of load, which vessel is without a separation unit.
  • a relevant method to reduce emission of CO is to deposit CO 2 in underground reservoirs from where hydrocarbons are produced, whereby the injected CO 2 contributes to maintenance of the reservoir pressure for continued production of hydrocarbons.
  • Said CO 2 is injected in liquid form or in gas form, of which injection in gas form currently goes on. The idea of injecting CO 2 in liquid form in underground reservoirs is known, and is planned at the Sn ⁇ hvitfeltet outside northern Norway from the year 2005.
  • a vessel is needed that can transport said loads on one keel under full flexibility with respect to load exchange, whereby LPG and condensate can be transported one way and liquid CO 2 can be transported another way. It is also demand for a vessel that, in addition to the above mentioned functions can be connected to gas fields without facilities for production of heavier gas components, such that on the vessel can the heavier gas components be separated out and loaded, while unloading of liquid CO 2 for subsequent underground injection takes place.
  • Figure 1 illustrates a vessel according to the invention, connected to a gas field.
  • Figure 2 illustrates a vessel according to the invention, connected to a power plant.
  • a vessel 1 comprising: equipment to load LPG, one or more tanks 2 for stable storage of LPG under transport, and equipment to unload LPG, equipment to load condensate or other liquid that is stable at atmospheric pressure, one or more tanks 3 for storage of said condensate or liquid under transport, and equipment to unload said condensate or liquid.
  • the vessel is distinguished in that it further is comprising: s Equipment to load liquid CO 2 , one or more tanks 4 for stable storage of liquid
  • a separation unit 6 capable to receive a flow 7 of wet gas and condensate for separation into LPG, condensate and dry gas, such that LPG and condensate can be o passed to respective tanks 2, 3 in the vessel and dry gas 8 can be passed out from the vessel to another unit.
  • FIG. 1 a vessel is illustrated, laying connected to a gas field off shore, via a surface platform that is without facilities for production of the heavier gas components.
  • the vessel is loading a flow 7 comprising wet gas and condensate for separation of said s load in the separation unit into LPG, condensate and dry gas.
  • LPG and condensate are stored at the vessel in respective tanks 2, 3, whereby the vessel is loaded with LPG and condensate.
  • the dry gas is passed through a line 8 back to the surface platform for subsequent further transport, for example through-a gas pipeline.
  • the connection to the gas field is via a connection of the type STL-Submerged Turret Loading, a submerged o rotatable body for loading, in agreement with the prior art.
  • the separation unit is preferably arranged close to the connection of the vessel to the gas field, to achieve a short transport distance.
  • Figure 1 illustrates the vessel and its operation in one end of the transport route. 5
  • Figure 2 the vessel and its operation in another end of the transport route is illustrated, more specific at a power work where the vessel loads liquid CO 2 and unloads
  • LPG liquidized petroleum gas that has to be cooled to a temperature below normal ambient temperature and/or be kept under pressure higher than 35 the atmospheric pressure t exist as a stable liquid.
  • condensate is meant the liquid components condensed from gas, and optionally smaller amounts of the components that in liquid form have been associated wit the gas, which condensate exists as a stable liquid at normal ambient temperature and atmospheric pressure.
  • CO 2 is meant in substance CO 2 , in such extent that the disturbing influence of further components is avoided.
  • the general construction or design of the vessel hull is preferably in agreement with the patent publication NO 2001 1982.
  • the vessel has double hull with a central loading area along the longitudinal axis of the vessel, between two longitudinal running outer bulk heads, preferably with loading tanks arranged in a row central along the longitudinal axis of the central loading area, and with side tanks or wing tanks symmetrically between said bulkheads and the outer double hull walls.
  • the vessel is comprising for example 8 tanks arranged along the central axis of the ship, which tanks have construction and equipment that allows anyone of the actual types of load, and tanks ' for condensate or another liquid stable at atmospheric pressure along each side of the vessel.
  • an arrangement is provided for fluid communication between tanks, preferably with double valve segregation.
  • the vessel can in general be constructed freely under the condition that the functions that are to be operated are maintained.
  • the tanks can in principle take any form and be of any number, provided that the function of the vessel is maintained.
  • the condensate tanks can be dimensioned for atmospheric pressure and atmospheric temperature
  • LPG-tanks can be dimensioned for minimum 3 bar operating pressure and maximum -30 °C operating temperature
  • CO 2 tanks can be dimensioned for minimum 5.3 bar operating pressure and maximum -50 °C operating temperature.
  • Most preferable tanks for any type of load are designed and equipped to maintain a loading temperature of -50 °C or lower and a pressure of minimum 8 bar.
  • all loading tanks of the vessel are according to said requirement, whereby all tanks can handle all actual types of load.
  • the tanks are conveniently constructed with outer isolation over a shell of austenitic stainless steel or another material not susceptible to brittle cracking at the actual cooling, with a cooling jacket between said isolation and shell, and optionally with means for cooling in the tanks.
  • each tank intended for any actual type of load has the form of a cylinder with circular cross-section with a half sphere formed upper end and a half sphere formed lower end, wherein each tank is arranged standing vertical in the vessel with the upper end above the deck level of the vessel.
  • Typical dimensions will be: inner diameter 8-10 m and height 15-20 .
  • Such tank design gives a preferable large storage volume with respect to wall thickness and weight of a tank.
  • all the tanks are formed as a vertical standing cylinder of circular cross-section and half sphere formed ends, of which the tanks arranged along the longitudinal axis of the vessel extend to over deck level while side tanks or wing tanks are completely below deck level synxmetrically arranged around the longitudinal axis of the vessel.
  • All types of load are present as liquid and are loaded and unloaded by use of pipes, connections, valves and pumps.
  • Preferably sinking pumps are used in the tanks to ensure good emptying. Provided that the tanks and equipment for loading and unloading are formed such that good emptying is achieved, it is not expected any problems by changing from one type of load to another in a tank.
  • the vessel has two independent cooling systems or cooling loops, with cooling to tanks, optionally to equipment for loading and unloading, and to the separation unit.
  • the loading and unloading equipment, tanks and the cooling parts of the separation unit are preferably cooled in advance before introducing LPG or CO 2 into tanks and CO 2 into the heat exchanger of the separation unit.
  • the inflow of wet gas to the vessel is at a typical pressure of 200-300 bar and a typical temperature of 100 °C .
  • the separation unit of the vessel is constructed such that it functions by expansion and pressure relief combined with cooling.
  • the cooling is completely or in part provided with heat exchange with relatively cold liquid CO 2 in a CO 2 flow that is unloaded to another unit, which liquid CO -flow that is unloaded is counter current to the inflow to the separation unit.
  • This is indicated on Figure 1 by conducting the CO 2 -flow 5 through a part of the separation unit 6.
  • Flow loops of liquid CO 2 for cooling in addition to the flow that is provided at unloading, can be arranged.
  • the separation unit of the vessel contains equipment for temperature controlled heat exchange with liquid CO 2 such that the temperature of the liquid CO is maintained below a predetermined maximum upper value. Thereby the formation of dry ice or CO 2 -gas in the heat exchanger can be avoided.
  • the heat exchanger is cooled in advance by use of the cooling system and or liquid CO 2 before the inlet flow to the separation unit gradually is opened.
  • a vessel is provided, which in principle is corresponding to the vessel described above, except that the vessel is without a separation unit.
  • the additional vessel is distinguished in that it is comprising: equipment to load LPG, one or more tanks 2 for stable storage of LPG under transport, and equipment to unload LPG, equipment to load condensate or another liquid that is stable under atmospheric pressure, one or more tanks 3 for storage of said condensate or liquid under transport, and equipment to unload said condensate or liquid, and equipment to load liquid CO 2 , one or more tanks 4 for stable storage of liquid CO 2 under transport, and equipment 5 to load liquid CO 2 to another unit, for example for subsequent injection into an underground reservoir.
  • the additional vessel cannot be connected to a gas field to separate out and load heavy gas components such as LPG and condensate, but can load LPG, condensate or another liquid that is stable at atmospheric pressure where such load is available separated and ready for shipping.
  • An actual transport way is to load liquid CO 2 from a gas work (for example Skogn, in Trondheimsfjorden, Mid-Norway), deliver said liquid CO at a LNG- plant (for example Sn ⁇ hvit) for subsequent injection into an underground reservoir, load LPG and condensate from said LNG-plant, and deliver said LPG and condensate at said gas work or another location, and reload liquid CO 2 from the gas work.
  • the additional vessel according to the invention has the same preferred embodiments and preferable features as those described for the previously described vessel, to the extent the vessels have similar design.
  • a system for energy production without emission of CO 2 to the atmosphere is provided, distinguished in that it is comprising one or more sources to hydrocarbons, one or more vessels, and optionally other transport units, for transport of said hydrocarbons to one or more power plants where energy is produced by combusting said hydrocarbons, and one or more sources to CO 2 that can be transported by the one or more vessels and optionally other transport units to one or more receiving stations for CO 2 for subsequent injection of CO 2 into the underground.
  • the source of the system for hydrocarbons and the receiving station for CO 2 for subsequent injection of CO 2 into the underground is one or more gas fields or facilities connected thereto, for example processing facilities.
  • the source to CO 2 is the combustion at the one or more power plants, naturally occurring CO 2 in said sources for hydrocarbons, and optionally additional sources such as refineries and industrial installations.
  • CO 2 is present as liquid before transport, whereby the transport volume is reduced.
  • CO 2 can also be transported and injected in form of gas.
  • Naturally occurring CO 2 amongst said sources for hydrocarbons can exist in mixture with said hydrocarbons, and can be transported in mixture with said hydrocarbons. The hydrocarbons are then combusted for energy production in the one or more power plants, whereafter all CO 2 is liquidized. If the CO 2 - admixture into the hydrocarbons is very high, a part of the CO 2 can be separated out before said combustion or additional hydrocarbons can be admixed.
  • vessels as described above, with embodiments as described, are utilized for the system according to the present invention.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Ocean & Marine Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Architecture (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Glass Compositions (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

L'invention concerne une cuve (1), comprenant: un équipement destiné à charger du LPG, un ou plusieurs réservoirs (2) permettant de stocker de façon stable du LPG lors de son transport, et un équipement permettant de charger du condensat ou un autre liquide stable sous pression atmosphérique, un ou plusieurs réservoirs (3) permettant de stocker ce condensat ou ce liquide lors de transports, et un équipement permettant de décharger ce condensat ou ce liquide. Cette cuve comprend également: un équipement permettant de charger le CO2, un ou plusieurs réservoirs (4) destinés à stocker le CO2 liquide de façon stable lors du transport, et un équipement (5) permettant de décharger le CO2 liquide dans une autre unité, par exemple en vue d'une injection dans un réservoir souterrain, une unité de séparation (6) permettant de recevoir un flux (7) de gaz humide et de condensat destiné à être séparé en LPG, condensat et gaz sec, de sorte que le LPG et le condensat puissent passer des réservoirs respectifs (2, 3) dans la cuve et que le gaz sec (8) puisse passer de la cuve vers une autre unité. L'invention concerne également une cuve supplémentaire à celle susmentionnée, ne comprenant pas d'unité de séparation. Cette invention concerne enfin un système permettant de produire de l'énergie sans émission de CO2 dans l'atmosphère.
PCT/NO2002/000442 2001-12-03 2002-11-26 Cuve destinee au transport de lpg et de co2 liquide et systeme de production d'energie sans emission de co2 dans l'atmosphere WO2003066423A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AU2002367607A AU2002367607A1 (en) 2001-12-03 2002-11-26 Vessel for transport of lpg and liquid co2 and system for energy production without emission of co2 to the atmosphere

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
NO20015889A NO324883B1 (no) 2001-12-03 2001-12-03 Fartoy
NO20015889 2001-12-03

Publications (1)

Publication Number Publication Date
WO2003066423A1 true WO2003066423A1 (fr) 2003-08-14

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AU (1) AU2002367607A1 (fr)
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WO2006008486A2 (fr) * 2004-07-16 2006-01-26 Statoil Asa Navire de transport de co2 liquefie
WO2006128470A2 (fr) * 2005-06-02 2006-12-07 Lauritzen Kozan A/S Equipement destine a un bateau-citerne transportant un produit hydrocarbone liquefie ou un produit analogue
WO2008009930A2 (fr) * 2006-07-18 2008-01-24 Ntnu Technology Transfer As Appareil et procédés pour le transport et le traitement de gaz naturel
WO2010145808A1 (fr) * 2009-06-16 2010-12-23 Tge Marine Gas Engineering Gmbh Procédé de réduction d'émission de dioxyde de carbone et dispositif associé
CN104203745A (zh) * 2012-03-22 2014-12-10 三星重工业有限公司 二氧化碳管理系统及方法
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WO2021124622A1 (fr) * 2019-12-19 2021-06-24 三菱造船株式会社 Navire
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JP2010266068A (ja) * 2004-07-16 2010-11-25 Statoil Asa 船
EA009263B1 (ru) * 2004-07-16 2007-12-28 Статойл Аса Судно
WO2006008486A3 (fr) * 2004-07-16 2006-03-16 Statoil Asa Navire de transport de co2 liquefie
JP2008506899A (ja) * 2004-07-16 2008-03-06 スタットオイル エイエスエイ 船
WO2006008486A2 (fr) * 2004-07-16 2006-01-26 Statoil Asa Navire de transport de co2 liquefie
NO340974B1 (no) * 2004-07-16 2017-07-31 Statoil Asa Fartøy
WO2006128470A2 (fr) * 2005-06-02 2006-12-07 Lauritzen Kozan A/S Equipement destine a un bateau-citerne transportant un produit hydrocarbone liquefie ou un produit analogue
WO2006128470A3 (fr) * 2005-06-02 2007-10-18 Lauritzen Kozan As Equipement destine a un bateau-citerne transportant un produit hydrocarbone liquefie ou un produit analogue
WO2008009930A2 (fr) * 2006-07-18 2008-01-24 Ntnu Technology Transfer As Appareil et procédés pour le transport et le traitement de gaz naturel
WO2008009930A3 (fr) * 2006-07-18 2009-01-15 Ntnu Technology Transfer As Appareil et procédés pour le transport et le traitement de gaz naturel
JP2012530239A (ja) * 2009-06-16 2012-11-29 テーゲーエー、マリン、ガス、エンジニヤリング、ゲーエムベーハー 二酸化炭素の排出を低減するための方法および装置
WO2010145808A1 (fr) * 2009-06-16 2010-12-23 Tge Marine Gas Engineering Gmbh Procédé de réduction d'émission de dioxyde de carbone et dispositif associé
CN104203745A (zh) * 2012-03-22 2014-12-10 三星重工业有限公司 二氧化碳管理系统及方法
US11725780B2 (en) 2017-01-31 2023-08-15 Nearshore Natural Gas, Llc Compressed natural gas storage and transportation system
CN110505977A (zh) * 2017-01-31 2019-11-26 近岸自然气体有限责任公司 压缩天然气存储和运输系统
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