EP1663786A1 - Gas offloading system - Google Patents

Gas offloading system

Info

Publication number
EP1663786A1
EP1663786A1 EP04784045A EP04784045A EP1663786A1 EP 1663786 A1 EP1663786 A1 EP 1663786A1 EP 04784045 A EP04784045 A EP 04784045A EP 04784045 A EP04784045 A EP 04784045A EP 1663786 A1 EP1663786 A1 EP 1663786A1
Authority
EP
European Patent Office
Prior art keywords
seafloor
floating structure
gas
onshore
electricity
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Withdrawn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
EP04784045A
Other languages
German (de)
French (fr)
Other versions
EP1663786A4 (en
Inventor
Jack Pollack
Hein Wille
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.)
Single Buoy Moorings Inc
Original Assignee
Single Buoy Moorings Inc
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
Priority claimed from US10/923,577 external-priority patent/US6973948B2/en
Application filed by Single Buoy Moorings Inc filed Critical Single Buoy Moorings Inc
Publication of EP1663786A1 publication Critical patent/EP1663786A1/en
Publication of EP1663786A4 publication Critical patent/EP1663786A4/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C1/00Pressure vessels, e.g. gas cylinder, gas tank, replaceable cartridge
    • F17C1/007Underground or underwater storage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323Valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323Valves
    • F17C2205/0332Safety valves or pressure relief valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0352Pipes
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0352Pipes
    • F17C2205/0364Pipes flexible or articulated, e.g. a hose
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/033Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/031Not under pressure, i.e. containing liquids or solids only
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033Small pressure, e.g. for liquefied gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2225/00Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0107Single phase
    • F17C2225/0123Single phase gaseous, e.g. CNG, GNC
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2225/00Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0146Two-phase
    • F17C2225/0153Liquefied gas, e.g. LPG, GPL
    • F17C2225/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2225/00Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/03Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
    • F17C2225/035High pressure, i.e. between 10 and 80 bars
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01Propulsion of the fluid
    • F17C2227/0128Propulsion of the fluid with pumps or compressors
    • F17C2227/0135Pumps
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01Propulsion of the fluid
    • F17C2227/0128Propulsion of the fluid with pumps or compressors
    • F17C2227/0157Compressors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0367Localisation of heat exchange
    • F17C2227/0369Localisation of heat exchange in or on a vessel
    • F17C2227/0376Localisation of heat exchange in or on a vessel in wall contact
    • F17C2227/0379Localisation of heat exchange in or on a vessel in wall contact inside the vessel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0367Localisation of heat exchange
    • F17C2227/0388Localisation of heat exchange separate
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2265/00Effects achieved by gas storage or gas handling
    • F17C2265/05Regasification
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2265/00Effects achieved by gas storage or gas handling
    • F17C2265/07Generating electrical power as side effect
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0102Applications for fluid transport or storage on or in the water
    • F17C2270/0105Ships
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0102Applications for fluid transport or storage on or in the water
    • F17C2270/011Barges
    • F17C2270/0113Barges floating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0102Applications for fluid transport or storage on or in the water
    • F17C2270/0118Offshore
    • F17C2270/0123Terminals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0134Applications for fluid transport or storage placed above the ground
    • F17C2270/0136Terminals
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0142Applications for fluid transport or storage placed underground
    • F17C2270/0144Type of cavity
    • F17C2270/0149Type of cavity by digging cavities
    • F17C2270/0152Salt caverns
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0142Applications for fluid transport or storage placed underground
    • F17C2270/0157Location of cavity
    • F17C2270/016Location of cavity onshore
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/01Applications for fluid transport or storage
    • F17C2270/0142Applications for fluid transport or storage placed underground
    • F17C2270/0157Location of cavity
    • F17C2270/0163Location of cavity offshore
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2270/00Applications
    • F17C2270/05Applications for industrial use
    • F17C2270/0581Power plants

Definitions

  • Hydrocarbons that are in a gaseous state at atmospheric pressure and room temperature are often transported as cold hydrocarbons, as by ship in liquid form such as LNG (liquified natural gas), at atmospheric pressure and - 160° C.
  • LNG liquid natural gas
  • Another form of cold gaseous hydrocarbons that are ship-transported are hydrates (gas entrapped in ice).
  • the LNG or other gas
  • the LNG may be heated and flowed to an onshore distribution facility.
  • Proposed prior art offloading stations have included a fixed platform extending up from the seafloor to a height above the sea surface and with a regas unit on the platform for heating the LNG.
  • a relatively low-cost system for offloading cold hydrocarbons, and especially LNG (liquified natural gas), and transporting the gas to an onshore gas distribution station.
  • the system includes a floating structure such as a barge at the sea surface that is moored so it weathervanes.
  • a tanker carrying LNG attaches itself to the floating structure so they weathervane together.
  • a regas unit which heats the LNG, usually by transferring heat from sea water, transforms the LNG into gas that can be more easily passed through moderate cost hoses or pipes and eventually to the onshore distribution station.
  • a new tanker arrives at the floating structure perhaps every week, and efforts are made to offload the tanker as fast as possible, perhaps in one day.
  • To provide a steady flow of gas to the onshore distribution station much of the rapidly- offloaded and regassed LNG is stored in an underground (and usually undersea) cavern.
  • the gas is slowly flowed from the cavern along a seafloor pipeline to the onshore distribution station, to provide a steady gas supply without requiring a large gas storage facility at the onshore station.
  • the regas unit and pumps for pressurizing gas are preferably electrically energized for safety and convenience. Electric power on the order of 60 megawatts may be required. Such electrical energy can be obtained from a power generator apparatus on the floating structure that uses gas from the tanker for fuel.
  • the regas unit may require electric power only part of the time, such as one day per week when LNG is being offloaded and regassed.
  • the rest of the time e.g. several days per week
  • electric power from the power generator apparatus is passed through a seafloor electric power line to an onshore electric distribution facility.
  • the generation of electric power at the floating structure is economical because the gas fuel is already available and because a large amount of expensive land is not required to isolate the power generation apparatus from onshore homes and businesses for safety. Electric power instead can be obtained from an onshore electric power distribution facility. In that case, an electric power line extends from the onshore facility and along the seafloor and up to the floating structure.
  • Fig. 1 is a partially sectional side view of an offshore gas offloading and transfer system of a first embodiment of the invention.
  • Fig. 1 A is a plan view of a portion of the system of Fig. 1.
  • Fig. 1 B is a plan view of a portion of a system that is a variation of Fig. 1 A.
  • Fig. 2 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 3 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 4 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 1 A is a plan view of a portion of the system of Fig. 1.
  • Fig. 1 B is a plan view of a portion of a system that is a variation of Fig. 1 A.
  • Fig. 2 is a partially sectional side view of an offshore gas
  • FIG. 5 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 6 is a top isometric view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 7 is a sectional side view of the system of Fig. 6.
  • Fig. 8 is a sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
  • Fig. 1 illustrates an offloading and transfer system 10 that includes a weathervaning floating structure in the form of a single barge 12 (there could be more than one barge) that floats at the sea surface 15.
  • the barge receives LNG through a coupling 17 and a loading arm 11 extending from midship of a tanker 13.
  • the barge is moored to the seafloor 14 by chains 16 extending from a turret 20 mounted at the bow of the barge.
  • the illustrated chains extend in catenary curves to the seafloor and along the seafloor to anchors.
  • the tanker is moored to the barge and they weathervane together.
  • a regas unit 22 for heating LNG to produce gas
  • an injection unit 24 for pumping the LNG or gas to a high pressure
  • the regas unit usually transfers heat from seawater to the LNG to change it into gas.
  • a flexible riser 32 (there often can be two or more) extends up from a platform 34 on the seafloor to the barge. The platform is connected through a pipe 36 to the cavern 30 in which the pressured gas is stored, that results from heating LNG.
  • a pipeline 40 extends primarily along the seafloor to an onshore gas distribution station 42.
  • the onshore station can be a gas grid that distributes the gas to users, can be a power plant that distributes the gas to gas turbines, etc..
  • the flexible riser 32 and connections 50, 52 at its opposite ends, can be made highly reliable.
  • reliable shutoff valves are present at 54 on the platform and on the barge.
  • large numbers of flexible risers have been designed, constructed and used in offshore installations to produce hydrocarbons (usually including gas and liquid) from undersea reservoirs. Experience gained from such use has resulted in high reliability.
  • applicant is able to achieve the same high standards of reliability previously achieved with fixed platforms, but at far lower cost. Fig.
  • FIG. 1A shows a combination 62 of the tanker 13 and barge 12 held together to weathervane together about the turret axis 56.
  • Fig. 1 B shows another combination 64 where the tanker moored to the barge by a hawser 60, so they weathervane together.
  • Fig. 2 shows an offloading/injection system 70 similar to that of Fig. 1 , except that two risers 72, 74 are shown.
  • One riser 72 connects to a pipe 76 that extends to the cavern 30.
  • the other riser 74 connects directly to a seafloor pipeline 80 that extends to the onshore station 82.
  • a break is indicated at 83 to indicate that the pipeline may be long (e.g. over one kilometer).
  • a pressure boosting unit 84 on the barge 90 can pressurize gas that is pumped through the pipeline 80. Such pressured gas is directed through valves in the onshore station 82 but the gas does not have to be pressurized by the onshore station. This keeps the pumps at 84 far from any inhabited structures on shore.
  • some of the offloaded gas is injected via riser 72 into the cavern 30 while other gas is transferred through riser 74 to the shore station.
  • gas is removed from the cavern via the riser 72, its pressure is boosted by pressure boosting unit 84, and sent to the shore station via riser 74.
  • riser 72 is used bi-directionally.
  • Fig. 3 shows a system 100 in which the barge 102 injects LNG directly into the cavern through a cryogenic pipeline or flexible pipe 104 that connects to a conduit 105.
  • the LNG gradually changes into its gas phase.
  • Gas is withdrawn through a separate pipe 112 leading from an upper portion of the cavern to a seafloor pipeline 110 that extends to an onshore station 114.
  • all gas from the barge passes through a seafloor pipeline 120 to an onshore station 122 that injects it into a cavern 124 that is directly connected to the onshore station.
  • Fig. 3 shows a system 100 in which the barge 102 injects LNG directly into the cavern through a cryogenic pipeline or flexible pipe 104 that connects to a conduit 105.
  • the LNG gradually changes into its gas phase.
  • Gas is withdrawn through a separate pipe 112 leading from an upper portion of the cavern to a seafloor pipeline 110 that extends to an onshore station 114.
  • all gas from the barge passes through
  • cold LNG is pumped from the barge 130 through a cryogenic hose or pipeline riser 132, and passes through a cryogenic seafloor pipeline 134 directly into an onshore injector and regas unit 136 that connects through pipe 138 to the cavern 140.
  • the injector 136 can inject LNG or can regas some or all of the LNG before injection, depending upon the expected rate of gas withdrawal and the amount already stored in the cavern.
  • Gas is removed from the cavern through a separate pipe 142 leading to another onshore station 144.
  • Fig. 6 illustrate another offloading station 150 for offloading gaseous hydrocarbons from a tanker 152.
  • the tanker 152 carries the hydrocarbons as LNG at -165°C and atmospheric pressure.
  • the station includes a direct-attachment floating structure 154.
  • the direct-attachment floating structure includes a buoyancy-adjusting floating system 160 and a propulsion system 162 that allows the floating structure to lie low in the water, slowly propel itself until its under-tanker part 164 lies under the tanker, and then deballast itself (by emptying water from ballast tanks) until its parts 164, 166 engage the tanker.
  • Such a structure has been previously used in offloading crude oil from tankers.
  • the particular floating structure 154 of Fig. 6 also includes a regas system 170 that warms the LNG so it becomes gaseous.
  • the floating structure pumps the gaseous hydrocarbons through a riser 172 into a subsea cavern and/or through a pipeline to a shore station.
  • Fig. 6 shows that a seafloor base 174 carries a fluid swivel 176.
  • a hawser 180 that extends from a yoke 182 attached to the swivel, extends to the bow 184 of the tanker to moor the tanker so it weathervanes.
  • the structure 154 weathervanes with the tanker. Energy is required to power the propulsion and ballast systems, as well as the regas systems.
  • the regas system will use pumped seawater, as to warm an intermediate liquid that warms LNG or even to directly warm the LNG to produce hydrocarbons in a gaseous state.
  • the hydrocarbons are pumped into a cavern 191 (Fig. 7) and/or a seafloor gas pipeline 190 that extends to an onshore gas facility 192.
  • power can be obtained from a power line 194 shown in Fig. 7.
  • the power line preferably extends parallel to the pipeline.
  • the shore end 196 of the power line can be connected to an on shore electric power facility such as a utility electric line 200, or to a special shore based power station.
  • the floating structure shown in Fig. 6 as well as Figs. 1-5 may consume on the order of magnitude of 60 megawatts (e.g. up to 200 Mw) of electricity when unloading a tanker.
  • a power line to shore is most practical when the seafloor base lies within about fifty kilometers (less than 70km) of shore so there are only moderate power losses along the power line.
  • the power line preferably lies partially on the seafloor. In most cases the floating structure lies at least 50 meters from shore in its greatest excursion, and the seafloor platform lies at least 50 meters from shore (high tide). It is also possible to provide a small power plant (e.g. 60 Mw), indicated at 201 in Fig. 7, which uses a small portion (much less than 50%) of the warmed gas as fuel to continually produce electric power.
  • the power is used perhaps one day in five or seven primarily to pump sea water in the heat exchanger and to pressurize gas.
  • Fig. 8 illustrates a system 210 which includes a floating structure 212 that is moored through its turret 214 to the seafloor.
  • a riser (one or more risers) 216 carries gas to a seafloor reservoir 220 and to a pipeline 222 that extends along the seafloor to shore.
  • An electric power line 224 that extends primarily along the seafloor, extends from the turret and over a buoy 226 and along the seafloor 226 to a facility on shore.
  • the floating structure carries a gas-powered generator 230 that generates electricity for energizing a unit 231 for regasing (heating) LNG from a tanker (not shown) as by pumping sea water through a heat exchanger, and for pressurizing the gas.
  • a switch arrangement 232 diverts the generated electric power through line 224 to an onshore facility at P, as to add to electricity generated by a local electric utility. Electricity can instead be transferred from a local utility to the power line to power equipment.
  • the riser can be constructed to be disconnected from the floating structure, and laid down on the seafloor or floated in a submerged position.
  • the floating structure can be disconnected from the riser and from its mooring system, and can be towed away, to be later reinstalled.
  • the invention provides a gas offloading and transfer system for transferring gas from a tanker (wherein the gas is stored in a liquid-like state such as LNG) to an undersea or underground cavern and/or to the shore.
  • the system can be constructed at moderate cost even when it must lie in a sea of considerable depth.
  • the system includes a floating structure such as a barge, which is moored, as by catenary chains, to the seafloor. In most cases the floating structure is moored so it weathervanes, to change direction so as to always face the sea in the direction of least resistance.
  • a tanker that brings the gas to the barge is moored to weathervane with the floating structure, so the tanker and floating structure can remain attached to one another during offloading in the open sea.
  • a weathervaning tanker could not be easily moored to a fixed platform in an open sea.
  • the floating structure is a weathervaning barge.
  • the floating structure is a direct attachment floating structure that, by itself, may not have a bow end that turns to always faces upwind, but which attaches to a tanker that is moored and thereby weathervanes with the tanker.
  • An electric current- carrying power cable can extend between the floating structure and a shore-based electric power structure, to deliver electric power to the floating structure to energize pumps and other equipment, or to carry electricity from a power plant on the floating structure to shore when not used at the floating structure.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Supply And Distribution Of Alternating Current (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)

Abstract

A system (10) is described for offloading LNG (liquified natural gas) from a tanker (13) for eventual delivery to an onshore gas distribution station (42). The system includes a floating structure (12) that floats at the sea surface and that is connected to the tanker so they weathervane together. The floating structure carries a regas unit (22) that heats the LNG to produce gas, and delivers the gas through a riser (32) to an underground cavern (30) that stores the gas. Gas from the cavern is delivered through a seafloor pipeline (40) to an onshore gas distribution station. The regas unit includes water pumps and other equipment that is powered by electricity. The electricity can be obtained from an electric generator (200) on the floating structure, with surplus electricity delivered through a seafloor electric power line (194) that extends at least partially along the seafloor to an onshore electricity distribution facility (192). The electricity can instead be obtained by delivery from an onshore facility though a seafloor electric power line that extends up to the floating structure and to the regas unit.

Description

GAS OFFLOADING SYSTEM
BACKGROUND OF THE INVENTION Hydrocarbons that are in a gaseous state at atmospheric pressure and room temperature (e.g. 20° C), are often transported as cold hydrocarbons, as by ship in liquid form such as LNG (liquified natural gas), at atmospheric pressure and - 160° C. Another form of cold gaseous hydrocarbons that are ship-transported are hydrates (gas entrapped in ice). At the ship's destination, the LNG (or other gas) may be heated and flowed to an onshore distribution facility. Proposed prior art offloading stations have included a fixed platform extending up from the seafloor to a height above the sea surface and with a regas unit on the platform for heating the LNG. Because of fire dangers in dealing with LNG, rigid platforms, which minimize flexing joints, have previously been proposed for offloading LNG from a tanker and heating it to gasify it. The cost of a fixed platform is high even at moderate depths, and at increasing depths (e.g. over 50 meters) the costs of fixed platforms increase dramatically. In addition, if the platform lies in an open sea it is difficult to moor a tanker to the platform because the tanker shifts position and heading with changing winds, waves and currents. An offshore LNG offloading and regas station which avoided the use of fixed platforms, and which provided the high reliability demanded in LNG offloading, heating and storage, would lower the cost of such stations and allow them to be used in situations where they previously were uneconomical.
SUMMARY OF THE INVENTION In accordance with one embodiment of the present invention, a relatively low-cost system is provided for offloading cold hydrocarbons, and especially LNG (liquified natural gas), and transporting the gas to an onshore gas distribution station. The system includes a floating structure such as a barge at the sea surface that is moored so it weathervanes. A tanker carrying LNG attaches itself to the floating structure so they weathervane together. A regas unit which heats the LNG, usually by transferring heat from sea water, transforms the LNG into gas that can be more easily passed through moderate cost hoses or pipes and eventually to the onshore distribution station. A new tanker arrives at the floating structure perhaps every week, and efforts are made to offload the tanker as fast as possible, perhaps in one day. To provide a steady flow of gas to the onshore distribution station, much of the rapidly- offloaded and regassed LNG is stored in an underground (and usually undersea) cavern. The gas is slowly flowed from the cavern along a seafloor pipeline to the onshore distribution station, to provide a steady gas supply without requiring a large gas storage facility at the onshore station. The regas unit and pumps for pressurizing gas, are preferably electrically energized for safety and convenience. Electric power on the order of 60 megawatts may be required. Such electrical energy can be obtained from a power generator apparatus on the floating structure that uses gas from the tanker for fuel. The regas unit may require electric power only part of the time, such as one day per week when LNG is being offloaded and regassed. The rest of the time (e.g. several days per week) electric power from the power generator apparatus is passed through a seafloor electric power line to an onshore electric distribution facility. The generation of electric power at the floating structure is economical because the gas fuel is already available and because a large amount of expensive land is not required to isolate the power generation apparatus from onshore homes and businesses for safety. Electric power instead can be obtained from an onshore electric power distribution facility. In that case, an electric power line extends from the onshore facility and along the seafloor and up to the floating structure. The novel features of the invention are set forth with particularity in the appended claims. The invention will be best understood from the following description when read in conjunction with the accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a partially sectional side view of an offshore gas offloading and transfer system of a first embodiment of the invention. Fig. 1 A is a plan view of a portion of the system of Fig. 1. Fig. 1 B is a plan view of a portion of a system that is a variation of Fig. 1 A. Fig. 2 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention. Fig. 3 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention. Fig. 4 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention. Fig. 5 is a partially sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention. Fig. 6 is a top isometric view of an offshore gas offloading and transfer system of another embodiment of the invention. Fig. 7 is a sectional side view of the system of Fig. 6. Fig. 8 is a sectional side view of an offshore gas offloading and transfer system of another embodiment of the invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Fig. 1 illustrates an offloading and transfer system 10 that includes a weathervaning floating structure in the form of a single barge 12 (there could be more than one barge) that floats at the sea surface 15. The barge receives LNG through a coupling 17 and a loading arm 11 extending from midship of a tanker 13. The barge is moored to the seafloor 14 by chains 16 extending from a turret 20 mounted at the bow of the barge. The illustrated chains extend in catenary curves to the seafloor and along the seafloor to anchors. Preferably, the tanker is moored to the barge and they weathervane together. This allows the barge and tanker to move in unison and therefore remain close together in an open sea. A regas unit 22 (for heating LNG to produce gas) and an injection unit 24 for pumping the LNG or gas to a high pressure, are both located on the barge, and are used for injection of gas into an underground cavern 30 that lies under the sea. The regas unit usually transfers heat from seawater to the LNG to change it into gas. A flexible riser 32 (there often can be two or more) extends up from a platform 34 on the seafloor to the barge. The platform is connected through a pipe 36 to the cavern 30 in which the pressured gas is stored, that results from heating LNG. A pipeline 40 extends primarily along the seafloor to an onshore gas distribution station 42. The onshore station can be a gas grid that distributes the gas to users, can be a power plant that distributes the gas to gas turbines, etc.. The flexible riser 32 and connections 50, 52 at its opposite ends, can be made highly reliable. In addition, reliable shutoff valves are present at 54 on the platform and on the barge. During the past forty years or so, large numbers of flexible risers have been designed, constructed and used in offshore installations to produce hydrocarbons (usually including gas and liquid) from undersea reservoirs. Experience gained from such use has resulted in high reliability. By using such reliable flexible risers and shutoff valves in the present floating offloading and injection station, applicant is able to achieve the same high standards of reliability previously achieved with fixed platforms, but at far lower cost. Fig. 1A shows a combination 62 of the tanker 13 and barge 12 held together to weathervane together about the turret axis 56. Fig. 1 B shows another combination 64 where the tanker moored to the barge by a hawser 60, so they weathervane together. Fig. 2 shows an offloading/injection system 70 similar to that of Fig. 1 , except that two risers 72, 74 are shown. One riser 72 connects to a pipe 76 that extends to the cavern 30. The other riser 74 connects directly to a seafloor pipeline 80 that extends to the onshore station 82. A break is indicated at 83 to indicate that the pipeline may be long (e.g. over one kilometer). A pressure boosting unit 84 on the barge 90 can pressurize gas that is pumped through the pipeline 80. Such pressured gas is directed through valves in the onshore station 82 but the gas does not have to be pressurized by the onshore station. This keeps the pumps at 84 far from any inhabited structures on shore. During regasification of LNG on a vessel and offloading of gas from the vessel, some of the offloaded gas is injected via riser 72 into the cavern 30 while other gas is transferred through riser 74 to the shore station. When no LNG is being offloaded, gas is removed from the cavern via the riser 72, its pressure is boosted by pressure boosting unit 84, and sent to the shore station via riser 74. Thus, riser 72 is used bi-directionally. Fig. 3 shows a system 100 in which the barge 102 injects LNG directly into the cavern through a cryogenic pipeline or flexible pipe 104 that connects to a conduit 105. In the cavern 106 the LNG gradually changes into its gas phase. Gas is withdrawn through a separate pipe 112 leading from an upper portion of the cavern to a seafloor pipeline 110 that extends to an onshore station 114. In Fig. 4, all gas from the barge passes through a seafloor pipeline 120 to an onshore station 122 that injects it into a cavern 124 that is directly connected to the onshore station. In Fig. 5, cold LNG is pumped from the barge 130 through a cryogenic hose or pipeline riser 132, and passes through a cryogenic seafloor pipeline 134 directly into an onshore injector and regas unit 136 that connects through pipe 138 to the cavern 140. The injector 136 can inject LNG or can regas some or all of the LNG before injection, depending upon the expected rate of gas withdrawal and the amount already stored in the cavern. Gas is removed from the cavern through a separate pipe 142 leading to another onshore station 144. Fig. 6 illustrate another offloading station 150 for offloading gaseous hydrocarbons from a tanker 152. The tanker 152 carries the hydrocarbons as LNG at -165°C and atmospheric pressure. The station includes a direct-attachment floating structure 154. The direct-attachment floating structure includes a buoyancy-adjusting floating system 160 and a propulsion system 162 that allows the floating structure to lie low in the water, slowly propel itself until its under-tanker part 164 lies under the tanker, and then deballast itself (by emptying water from ballast tanks) until its parts 164, 166 engage the tanker. Such a structure has been previously used in offloading crude oil from tankers. The particular floating structure 154 of Fig. 6 also includes a regas system 170 that warms the LNG so it becomes gaseous. The floating structure pumps the gaseous hydrocarbons through a riser 172 into a subsea cavern and/or through a pipeline to a shore station. By regasing LNG, applicant avoid the need to provide a cryogenic riser which may be very expensive. Fig. 6 shows that a seafloor base 174 carries a fluid swivel 176. A hawser 180 that extends from a yoke 182 attached to the swivel, extends to the bow 184 of the tanker to moor the tanker so it weathervanes. The structure 154 weathervanes with the tanker. Energy is required to power the propulsion and ballast systems, as well as the regas systems. The regas system will use pumped seawater, as to warm an intermediate liquid that warms LNG or even to directly warm the LNG to produce hydrocarbons in a gaseous state. The hydrocarbons are pumped into a cavern 191 (Fig. 7) and/or a seafloor gas pipeline 190 that extends to an onshore gas facility 192. Where the floating structure lies near shore (e.g. not much more than fifty kilometers from shore), power can be obtained from a power line 194 shown in Fig. 7. The power line preferably extends parallel to the pipeline. The shore end 196 of the power line can be connected to an on shore electric power facility such as a utility electric line 200, or to a special shore based power station. The floating structure shown in Fig. 6 as well as Figs. 1-5, may consume on the order of magnitude of 60 megawatts (e.g. up to 200 Mw) of electricity when unloading a tanker. A power line to shore is most practical when the seafloor base lies within about fifty kilometers (less than 70km) of shore so there are only moderate power losses along the power line. The power line preferably lies partially on the seafloor. In most cases the floating structure lies at least 50 meters from shore in its greatest excursion, and the seafloor platform lies at least 50 meters from shore (high tide). It is also possible to provide a small power plant (e.g. 60 Mw), indicated at 201 in Fig. 7, which uses a small portion (much less than 50%) of the warmed gas as fuel to continually produce electric power. The power is used perhaps one day in five or seven primarily to pump sea water in the heat exchanger and to pressurize gas. During the other 4 days out of 5 or 6 days out of 7, the power is sent to shore along the power line 194. Fig. 8 illustrates a system 210 which includes a floating structure 212 that is moored through its turret 214 to the seafloor. A riser (one or more risers) 216 carries gas to a seafloor reservoir 220 and to a pipeline 222 that extends along the seafloor to shore. An electric power line 224 that extends primarily along the seafloor, extends from the turret and over a buoy 226 and along the seafloor 226 to a facility on shore. The floating structure carries a gas-powered generator 230 that generates electricity for energizing a unit 231 for regasing (heating) LNG from a tanker (not shown) as by pumping sea water through a heat exchanger, and for pressurizing the gas. When not regasing or pumping, a switch arrangement 232 diverts the generated electric power through line 224 to an onshore facility at P, as to add to electricity generated by a local electric utility. Electricity can instead be transferred from a local utility to the power line to power equipment. In environments that are subject to occasional harsh weather conditions such as a heavy storm or hurricane, the riser can be constructed to be disconnected from the floating structure, and laid down on the seafloor or floated in a submerged position. The floating structure can be disconnected from the riser and from its mooring system, and can be towed away, to be later reinstalled. Thus, the invention provides a gas offloading and transfer system for transferring gas from a tanker (wherein the gas is stored in a liquid-like state such as LNG) to an undersea or underground cavern and/or to the shore. The system can be constructed at moderate cost even when it must lie in a sea of considerable depth. The system includes a floating structure such as a barge, which is moored, as by catenary chains, to the seafloor. In most cases the floating structure is moored so it weathervanes, to change direction so as to always face the sea in the direction of least resistance. A tanker that brings the gas to the barge is moored to weathervane with the floating structure, so the tanker and floating structure can remain attached to one another during offloading in the open sea. A weathervaning tanker could not be easily moored to a fixed platform in an open sea. In one system, the floating structure is a weathervaning barge. In another system, the floating structure is a direct attachment floating structure that, by itself, may not have a bow end that turns to always faces upwind, but which attaches to a tanker that is moored and thereby weathervanes with the tanker. An electric current- carrying power cable can extend between the floating structure and a shore-based electric power structure, to deliver electric power to the floating structure to energize pumps and other equipment, or to carry electricity from a power plant on the floating structure to shore when not used at the floating structure.

Claims

WHAT IS CLAIMED IS
1. An offshore gas unloading system (10, 70, 100, 150, 210) that lies in a sea having a sea surface (15) and a seafloor (14, 228), wherein a tanker (13, 152) unloads liquified cold hydrocarbons that are gaseous at room temperature, comprising: a floating structure (12, 90, 102, 130, 154, 212) that lies at the sea surface and that is moored so it weathervanes; a regas unit (22, 170) on said floating structure, that heats at least some of the cold hydrocarbons that were received from the tanker; a seafloor platform (34, 174) that lies at the seafloor; a riser (32, 132, 172, 216) that extends from said floating structure to said seafloor platform to carry hydrocarbons from one to the other; said floating structure being connected to said tanker to form a combination (60, 62) of said floating structure and said tanker that weathervane together; at least one mooring line (16) that extends from the seafloor to said combination to moor the combination and allow it to weathervane.
2. The system described in claim 1 including: an underground cavern (30, 106, 124, 140, 191 , 220) and a pipe (36, 76, 138) that is coupled to said cavern and to said riser, to thereby store at least some of the gas in the cavern.
3. The system described in claim 2 including: an onshore gas distribution station (42, 82, 114, 122, 144, 192); a seafloor pipeline (40, 80, 100, 120, 134, 190, 222) that is coupled to said cavern and that extends primarily along the seafloor from said cavern to said onshore station to carry said gas from said cavern to said onshore station.
4. The system described in claim 2 including: an onshore gas distribution station (82); a second riser (74) extending from said floating structure to seafloor; a seafloor pipeline (80) that extends primarily along the seafloor from a lower end of said second riser to said onshore station, whereby to enable the passage of gas into said cavern or directly to said onshore station without passing through said cavern.
5. The system described in claim 2 including: an onshore gas distribution station (114); said riser comprises a cryogenic hose (104), and including a conduit (105) that carries some of the cold hydrocarbons received by the floating structure, directly to the cavern (106) without passing through said regas unit so liquid cold hydrocarbons pass down through said cryogenic hose; said cavern has upper and lower portions, and including a seafloor gas pipeline (110) that has a proximal end (112) coupled to said cavern upper portion to receive gas therefrom, said pipeline extending to said onshore station.
6. The system described in claim 1 wherein: said regas unit is electrically energized; and including an electric generator apparatus (200, 230) mounted on said floating structure, which is fueled by gas from said regas unit and that generates electricity to energize said regas unit.
7. The system described in claim 6 including: an onshore electric power distributing facility (200); an electric current-carrying power line (194, 224) extending from said electric generator apparatus to the seafloor and along the seafloor to said onshore facility for carrying power to said onshore facility when such power is not required at the floating structure.
8. The system described in claim 1 wherein: said regas unit is electrically energized; and including an onshore power distributing facility (200); an electric current-carrying power line (194, 224) that extends along the seafloor from said onshore facility to a location under said floating structure and up through the sea to said floating structure to carry electric power to said regas unit.
9. A method for operating an offshore facility that lies off shore, and that unloads cold hydrocarbons from a tanker, for delivery of the hydrocarbons after warming, to a shore station on the shore, comprising: offloading cold hydrocarbons from the tanker to a floating structure that has a regas unit and an injection unit, passing said cold hydrocarbons through said regas unit to produce warmed gaseous hydrocarbons and passing the gaseous hydrocarbons through the injection unit to pressurize them; flowing said gaseous hydrocarbons to said shore station; said floating structure has a turret, and including mooring said floating structure to the seafloor with a plurality of mooring lines extending from said turret to the seafloor; coupling said tanker to said floating structure to form a combination that weathervanes as a combination.
10. The method described in claim 8 including: flowing at least some of said gaseous hydrocarbons to an underground cavern for storage, and flowing gaseous hydrocarbons from said cavern to said shore station.
11. The method described in claim 8 including: powering said regas unit and said injection unit with electricity and obtaining electricity from an electricity generator on said floating structure.
12. The method described in claim 11 including: passing electricity from said generator to an on-shore distribution station when electricity is not all needed to power said regas and injection units.
13. The method described in claim 8 including: powering said regas unit and said injection unit with electricity, and obtaining electricity from an onshore facility through a power line that extends at least partially along the seafloor.
14. An offshore gas unloading system (150, 210) that lies in a sea that has a seafloor and a sea surface, and that lies within about fifty kilometers of a shore, for unloading cold hydrocarbons from a tanker (152), comprising: a floating structure (154, 212) that lies at the sea surface and that has a fluid coupling for receiving said liquid cold hydrocarbons from said tanker; a cavern (191 , 220) that stores gas; a seafloor platform (174) and at least one pipe that extends from said seafloor platform to said cavern; at least one riser (172, 216) that extends from said floating structure to said seafloor platform and that is coupled to said pipe to carry hydrocarbons between said sea-surface structure and said cavern; said floating structure carrying an electrically powered equipment including a regas unit (170, 231); an electric power facility (200, P) that lies on the shore; a current carrying power line (194, 224) that extends between said sea- surface structure and said electric power facility on the shore, to carry electricity between them.
15. The system described in claim 14 including: an electricity generator (201 , 230) mounted on said floating structure that supplies electricity to said equipment, and an electric switch arrangement (232) that delivers electricity from said generator to said power line when much of the electricity is not required for said equipment.
16. The system described in claim 14 wherein: said electric power facility that lies on the shore is constructed to deliver electrical power to said power line, to provide electrical power to energize said equipment.
17. A method for operating an offshore facility that lies off shore, and that unloads cold hydrocarbons from a tanker, for delivery of the hydrocarbons after warming, to a shore station on the shore, comprising: offloading cold hydrocarbons from the tanker to a floating structure that has a regas unit, and passing said cold hydrocarbons through said regas unit to produce warmed gaseous hydrocarbons; flowing said warmed gaseous hydrocarbons to said shore station; including energizing said regas unit with electricity.
18. The method described in claim 17 including: using some of said warmed gaseous hydrocarbons to fuel an electrical generator apparatus on said floating structure to generate enough electric power to energize said regas unit and pressurize gas; delivering electricity from said electrical generator apparatus along a seafloor electric power line to an onshore facility when excess electric power is available from said electric generator apparatus.
19. The method described in claim 17 including: delivering electricity from an onshore facility along a seafloor electric power line to said floating structure to energize said regas unit with electric power from the onshore facility.
EP04784045.9A 2003-09-19 2004-09-15 Gas offloading system Withdrawn EP1663786A4 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US50444903P 2003-09-19 2003-09-19
US10/923,577 US6973948B2 (en) 2003-09-19 2004-08-20 Gas offloading system
PCT/US2004/030052 WO2005032942A1 (en) 2003-09-19 2004-09-15 Gas offloading system

Publications (2)

Publication Number Publication Date
EP1663786A1 true EP1663786A1 (en) 2006-06-07
EP1663786A4 EP1663786A4 (en) 2015-02-25

Family

ID=34425950

Family Applications (1)

Application Number Title Priority Date Filing Date
EP04784045.9A Withdrawn EP1663786A4 (en) 2003-09-19 2004-09-15 Gas offloading system

Country Status (6)

Country Link
EP (1) EP1663786A4 (en)
CN (1) CN1852832B (en)
BR (1) BRPI0414561B1 (en)
CA (1) CA2537496C (en)
MX (1) MXPA06003074A (en)
WO (1) WO2005032942A1 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NO20050856L (en) * 2005-02-17 2006-08-18 Statoil Asa System and procedure for offshore unloading and regasification of LNG
KR101121721B1 (en) * 2010-01-28 2012-02-28 에스티엑스조선해양 주식회사 Floating type LNG regasification unit
SG185008A1 (en) 2010-05-20 2012-11-29 Excelerate Energy Ltd Partnership Systems and methods for treatment of lng cargo tanks
NO341820B1 (en) * 2016-05-18 2018-01-29 Blystad Energy Man As Natural gas power plant arrangement
JP2018034668A (en) * 2016-08-31 2018-03-08 三菱重工業株式会社 Gas transfer facility and power generation facility
KR20240033113A (en) * 2018-06-01 2024-03-12 스틸헤드 엘엔지 (에이에스엘엔지) 엘티디. Liquefaction apparatus, methods, and systems
CN115075879B (en) * 2022-06-24 2023-07-21 中国矿业大学 Hydrogen storage structure based on composite reinforcement of deep underground rock cavern and construction method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6298671B1 (en) * 2000-06-14 2001-10-09 Bp Amoco Corporation Method for producing, transporting, offloading, storing and distributing natural gas to a marketplace
WO2002095284A1 (en) * 2001-05-23 2002-11-28 Exmar Offshore Company Method and apparatus for offshore lng regasification
US6517286B1 (en) * 2001-02-06 2003-02-11 Spectrum Energy Services, Llc Method for handling liquified natural gas (LNG)
WO2003049994A1 (en) * 2001-12-12 2003-06-19 Single Buoy Moorings Inc. Weathervaning lng offloading system
EP1680619A2 (en) * 2003-10-30 2006-07-19 SBM-IMODCO, Inc. Lng tanker offloading in shallow waters

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2413536A1 (en) * 1977-12-30 1979-07-27 Inst Francais Du Petrole ANCHORING AND TRANSFER STATION FOR THE PRODUCTION OF OIL OFFSHORE OIL
US4299260A (en) * 1979-06-18 1981-11-10 Amtel, Inc. Hydrocarbon production terminal
US4301840A (en) * 1979-06-18 1981-11-24 Amtel, Inc. Fixed turret subsea hydrocarbon production terminal
CN1003781B (en) * 1985-04-01 1989-04-05 布隆·福斯造船公司 Anchorage and transferring liquid or gasous medium system on stern of oil tanker
CN1104358C (en) * 1997-12-18 2003-04-02 美国油田钻探公司 Offshore production and storage facility and method of installing same

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6298671B1 (en) * 2000-06-14 2001-10-09 Bp Amoco Corporation Method for producing, transporting, offloading, storing and distributing natural gas to a marketplace
US6517286B1 (en) * 2001-02-06 2003-02-11 Spectrum Energy Services, Llc Method for handling liquified natural gas (LNG)
WO2002095284A1 (en) * 2001-05-23 2002-11-28 Exmar Offshore Company Method and apparatus for offshore lng regasification
WO2003049994A1 (en) * 2001-12-12 2003-06-19 Single Buoy Moorings Inc. Weathervaning lng offloading system
EP1680619A2 (en) * 2003-10-30 2006-07-19 SBM-IMODCO, Inc. Lng tanker offloading in shallow waters

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
None *
See also references of WO2005032942A1 *

Also Published As

Publication number Publication date
CA2537496A1 (en) 2005-04-14
BRPI0414561A (en) 2006-11-07
CA2537496C (en) 2009-01-20
BRPI0414561B1 (en) 2021-01-26
CN1852832B (en) 2010-05-12
BRPI0414561A8 (en) 2017-06-27
WO2005032942A1 (en) 2005-04-14
MXPA06003074A (en) 2006-06-20
CN1852832A (en) 2006-10-25
EP1663786A4 (en) 2015-02-25

Similar Documents

Publication Publication Date Title
US6973948B2 (en) Gas offloading system
US6997643B2 (en) LNG tanker offloading in shallow water
KR100871406B1 (en) An offshore system and a method of offloading and heating for quick lng offloading
US7119460B2 (en) Floating power generation system
US20080011357A1 (en) LNG tanker offloading in shallow waters
US6517286B1 (en) Method for handling liquified natural gas (LNG)
US7836840B2 (en) Subsea cryogenic fluid transfer system
JP5360598B2 (en) Transport and transfer of fluid
AU2006241566B2 (en) Large distance offshore LNG export terminal with boil-off vapour collection and utilization capacities
CN101646597A (en) System for transferring fluids between floating vessels using flexible conduit and releasable mooring system
EP1618330B1 (en) A cargo evaporation device for use when unloading ships
CA2537496C (en) Gas offloading system
WO2006088371A1 (en) System and method for offshore offloading and regasification of LNG
CN100505998C (en) Floating power generation system
MXPA06004807A (en) Lng tanker offloading in shallow waters

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20060303

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
RIN1 Information on inventor provided before grant (corrected)

Inventor name: WILLE, HEIN

Inventor name: POLLACK, JACK

A4 Supplementary search report drawn up and despatched

Effective date: 20150128

RIC1 Information provided on ipc code assigned before grant

Ipc: B65B 1/04 20060101AFI20150122BHEP

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

17Q First examination report despatched

Effective date: 20170412

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: EXAMINATION IS IN PROGRESS

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20211012