WO2008085005A1 - Tank for holding a cryogenic liquid and a conduit assembly, and a system for effecting flow control and pressure management of a cryogenic liquid held in the tank - Google Patents
Tank for holding a cryogenic liquid and a conduit assembly, and a system for effecting flow control and pressure management of a cryogenic liquid held in the tank Download PDFInfo
- Publication number
- WO2008085005A1 WO2008085005A1 PCT/KR2008/000185 KR2008000185W WO2008085005A1 WO 2008085005 A1 WO2008085005 A1 WO 2008085005A1 KR 2008000185 W KR2008000185 W KR 2008000185W WO 2008085005 A1 WO2008085005 A1 WO 2008085005A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- conduit
- tank
- inner shell
- fill
- cryogenic liquid
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 59
- 230000000903 blocking effect Effects 0.000 claims 4
- 238000007599 discharging Methods 0.000 claims 1
- 238000007726 management method Methods 0.000 abstract description 6
- 238000013022 venting Methods 0.000 abstract description 4
- 239000003949 liquefied natural gas Substances 0.000 description 14
- 239000000446 fuel Substances 0.000 description 11
- 230000008878 coupling Effects 0.000 description 4
- 238000010168 coupling process Methods 0.000 description 4
- 238000005859 coupling reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000002828 fuel tank Substances 0.000 description 3
- 238000010276 construction Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 1
- 230000001747 exhibiting effect Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
Classifications
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- 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
-
- 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
- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
- F17C7/02—Discharging liquefied gases
-
- 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
- F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
-
- 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
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- 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
- F17C2201/035—Orientation with substantially horizontal 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
- F17C2201/056—Small (<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
- F17C2203/0391—Thermal insulations by vacuum
-
- 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
- F17C2203/0626—Multiple walls
- F17C2203/0629—Two walls
-
- 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
- F17C2205/0332—Safety valves or pressure relief valves
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- 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
- F17C2205/0335—Check-valves or non-return 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
- 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
- F17C2205/0338—Pressure regulators
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- 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
- F17C2205/0352—Pipes
-
- 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
- F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
-
- 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
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- 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
- F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
- F17C2223/042—Localisation of the removal point
- F17C2223/046—Localisation of the removal point in the liquid
- F17C2223/047—Localisation of the removal point in the liquid with a dip tube
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- 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
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
- F17C2225/0146—Two-phase
- F17C2225/0153—Liquefied gas, e.g. LPG, GPL
- F17C2225/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
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- 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
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/03—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
- F17C2225/035—High pressure, i.e. between 10 and 80 bars
-
- 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
- F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
- F17C2225/04—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by other properties of handled fluid after transfer
- F17C2225/042—Localisation of the filling point
- F17C2225/046—Localisation of the filling point in the liquid
- F17C2225/047—Localisation of the filling point in the liquid with a dip tube
-
- 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
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0309—Heat exchange with the fluid by heating using another fluid
- F17C2227/0311—Air heating
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- 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
- F17C2227/0388—Localisation of heat exchange separate
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- 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
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0408—Level of content in the vessel
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- 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
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/061—Level of content in the vessel
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- 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
- F17C2260/02—Improving properties related to fluid or fluid transfer
- F17C2260/021—Avoiding over pressurising
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- 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
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- 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
- F17C2260/035—Dealing with losses of fluid
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- 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
- F17C2270/0165—Applications for fluid transport or storage on the road
- F17C2270/0168—Applications for fluid transport or storage on the road by vehicles
Definitions
- the present invention is directed to an assembly for effecting filling, withdrawal and fill level control of a cryogenic liquid held in a tank and to a flow control and pressure management system for a cryogenic liquid. More particularly, the present invention is directed to such an assembly and system applied to a vehicle-mounted tank for receiving and holding a cryogenic liquid fuel and for delivering the liquid fuel to the vehicle engine.
- the liquids intended for transfer by the apparatus and method of this invention exist in a cryogenic state.
- the present invention is particularly adapted for, but not limited to, a vehicle-mounted tank for efficiently holding liquefied natural gas (LNG), or methane, and a control assembly for efficiently introducing the LNG into the tank and transferring the LNG to the vehicle engine.
- LNG liquefied natural gas
- Cryogenic containers that are designed and manufactured for end-use as vehicular fuel tanks used to store extremely cold liquids require a means to fill the container and deliver product from the container.
- LNG vehicle fuel tanks are of double wall construction.
- the inner shell a pressure vessel containing LNG fuel, is supported within the outer shell.
- Radiation shielding such as wraps of polyester sheet aluminized on both sides, is placed in the space between the inner and outer shells, and the space is placed under a high vacuum to provide particularly effective insulation between the inner shell and the ambient. Since LNG is a cryogenic fuel that boils at -258 0 F (at normal atmospheric pressure), the pressure vessel support structure must exhibit a very low conductive heat leak.
- Tank "heat leak” has a dramatic effect on the pressure temperature and density relationships of the LNG thus making it very difficult to control the fuel tank pressure and maintain consistent fuel quality for delivery to the engine.
- Low heat leak minimizes tank pressure build-up during vehicle non-operational time periods and prevents venting of fuel during a designed "no vent” standby time.
- LNG is a dynamic fuel exhibiting fluid characteristics that vary with pressure and corresponding amount of internal energy. These variable fluid characteristics coupled with a cryogenic liquid temperature of -258 0 F at normal atmospheric pressure necessitate specific equipment and a system design that will enable efficient introduction of LNG into the tank(s) with an effective control of fill level in the tank. Also, the system controls must maintain a specified fuel supply flow rate to a vehicle engine within a specified pressure range during all modes of vehicle operation.
- An object of the invention is to effect the fill of the tank, the delivery of liquid from the tank and achieve pressure management of the tank with a single line thus providing a multi- function capability and reducing the number of tank penetrations and therefore a significant reduction in heat transfer.
- vent return line serves as a device that provides an indication of when the tank is filled to the maximum allowable liquid level and will allow for the expansion of the LNG after the fill of the tank. This is accomplished by means of a tubular elbow welded to the end of the vent line serpentine tube in the interior of the tank, in a position perpendicular to the liquid surface of the LNG.
- An object fulfilled by the invention is that, due to improved thermal protection design, "liquid only” can be delivered from the tank, thus assuring consistent fuel quality and pressure from the tank to an external heat exchanger for vaporization and delivery to an engine.
- Another object of the present invention is to provide for the reliable installation of a capacitance gauge probe in combination with the liquid fill/withdrawal tube.
- the capacitance probe is attached to the entrant tube unit by fittings welded to the vertical portion of the fill/withdrawal tubing.
- a conduit assembly includes a pair of tubes 10, 12 that extend through an end wall of a tank 13 for a cryogenic liquid.
- a tank to which the conduit assembly is applicable is disclosed in U.S. Patent No. 6,880,719 Bl.
- the tank makes use of a double wall construction having an inner shell 14 that holds the liquid under pressure and an outer shell 16 that surrounds the inner shell and is spaced from it.
- a barrier to heat transfer into the inner shell is provided by an evacuated space 18 between the inner and outer shells.
- the tubes have a serpentine form and extend side-by-side horizontally within an upper region of the inner shell.
- the tubes extend through outer and inner housings 20, 22 forming an extension of the evacuated space between the inner and outer shells.
- the tubes extend through a closure plate 20a on the outer housing, through the evacuated space between the shells, through the inner housing and closure plate 22a and into an upper central region of the inner shell.
- One of the tubes 10, used for filling and withdrawal of liquid includes a vertical section 10a that extends toward the bottom of the inner shell and has an opening at its lower end, Located adjacent to the vertical section 10a of tube 10 is a liquid level capacitance gauge 24.
- the other tube 12 used for venting and fill level control, terminates in the upper central region of the inner shell at an elbow 12a with a downwardly facing opening 12b.
- An electrical lead 24a from the capacitance gauge 24 is shown extending through the vent tube.
- a cryogenic liquid from a bulk supply flowing through the fill tube enters the inner shell at the bottom.
- gases above the surface of the liquid can flow from the inner shell through the vent tube 12 and back to the bulk supply.
- liquid will flow through the vent tube back to the bulk supply.
- a gas pressure pad established above the surface of the liquid will prevent further rise of the liquid in the inner shell.
- the elbow 12a is located so that the downwardly facing opening is generally coincident with the fill level mandated by applicable codes. The position of the elbow also establishes the proper "ullage space" (tank space not occupied by liquid) in the container, to allow for expansion of the LNG after filling.
- FIGs. 3 and 4 show a preferred embodiment of a system for effecting flow control and pressure management of a cryogenic liquid held in a tank.
- An elbow 12a of third conduit 30 is coupled to the outer end of fill and withdrawal conduit 10 that communicates with the bottom of tank 13.
- the other end of third conduit 30 is coupled to an outer end of tank vent tube 12 via a passage in manifold 32.
- a pressure regulator 34 is disposed in third conduit 30 between its couplings with conduits 10 and 12.
- third conduit 30 forms a loop between fill and withdrawal conduit 10 and vent tube 12, and the pressure regulator 34 is interposed in the loop.
- the pressure regulator incorporates a normally closed valve that opens in response to a drop in pressure in third conduit 30 below a predetermined level.
- a pressure regulator found to be suitable for this application is RegO Products Part No. RG 125.
- Fourth conduit 36 for conducting vapor from the tank to a bulk supply is coupled to third conduit 30 via a passage in the manifold 32 a shut off valve 38 (normally open) is disposed in fourth conduit 36. Also, coupled to the manifold are primary and secondary relief valves 40, 42. Teed into third conduit 30 between the coupling with conduit 10 and the pressure regulator 34 are fifth conduit 44 which receives cryogenic liquid from a bulk supply (not shown), and sixth conduit 46 which conducts cryogenic liquid to a point of use, such as a vehicle engine (not shown). As shown, an accumulator 48 and a check valve 50 are also disposed in third conduit 30 between the regulator 34 and the coupling with sixth conduit 46. A shut-off valve 52 (normally open) is disposed in third conduit 30 between the couplings with fill and withdrawal conduits 10 and fifth conduit 44. A solenoid valve 54 is disposed in sixth conduit 46 to allow or block flow of liquid to a point of use.
- the regulator 34 will maintain a constant delivery pressure to an engine.
- the liquid level in the tank will fall and the pressure in third conduit 30 may also fall.
- the valve in the regulator 34 will open, liquid in the accumulator 48 will pass through check valve 50 and regulator 34 and into the third conduit 30 on the other side of the regulator.
- This section third of conduit 30 acts as a heat exchanger in which liquid in the conduit will be vaporized by heat from ambient, causing expansion of the fluid in the conduit which causes a pressure build.
- very small amounts of liquid passing through the check valve 50 and the regulator 34 effect a pressure build that returns the pressure in conduit to a required level.
- the regulator shuts off, stopping vaporization and pressure build-up. As liquid is forced from the tank, pressure in the tank begins to drop and the pressure build regulator again begins operating.
Abstract
A tank for a cryogenic liquid is fitted with a conduit assembly that provides for flow of the cryogenic liquid into and out of the tank, venting of the tank and control of the fill level in the tank. The conduit assembly includes serpentine tubes that extend into an upper region within the inner shell. Within the inner shell, one of the tubes extends downwardly to a lower opening and provides for liquid flow into and out the tank; the other tube has an end with a downwardly facing opening in the upper region whereby vapor can be conducted out of the tank and the fill level is established. A system for effecting pressure management of the cryogenic liquid in the tank includes a conduit network that provides for pressure build as pressure in the conduit network drops and provides for delivery of liquid only to, e.g., a vehicle engine.
Description
Description
TANK FOR HOLDING A CRYOGENIC LIQUID AND A
CONDUCT ASSEMBLY, AND A SYSTEM FOR EFFECTING
FLOW CONTROL AND PRESSURE MANAGEMENT OF A
CRYOGENIC LIQUID HELD IN THE TANK Technical Field
[1] The present invention is directed to an assembly for effecting filling, withdrawal and fill level control of a cryogenic liquid held in a tank and to a flow control and pressure management system for a cryogenic liquid. More particularly, the present invention is directed to such an assembly and system applied to a vehicle-mounted tank for receiving and holding a cryogenic liquid fuel and for delivering the liquid fuel to the vehicle engine. The liquids intended for transfer by the apparatus and method of this invention exist in a cryogenic state. The present invention is particularly adapted for, but not limited to, a vehicle-mounted tank for efficiently holding liquefied natural gas (LNG), or methane, and a control assembly for efficiently introducing the LNG into the tank and transferring the LNG to the vehicle engine. Background Art
[2] Cryogenic containers that are designed and manufactured for end-use as vehicular fuel tanks used to store extremely cold liquids require a means to fill the container and deliver product from the container. Typically, LNG vehicle fuel tanks are of double wall construction. The inner shell, a pressure vessel containing LNG fuel, is supported within the outer shell. Radiation shielding, such as wraps of polyester sheet aluminized on both sides, is placed in the space between the inner and outer shells, and the space is placed under a high vacuum to provide particularly effective insulation between the inner shell and the ambient. Since LNG is a cryogenic fuel that boils at -2580F (at normal atmospheric pressure), the pressure vessel support structure must exhibit a very low conductive heat leak. Tank "heat leak" has a dramatic effect on the pressure temperature and density relationships of the LNG thus making it very difficult to control the fuel tank pressure and maintain consistent fuel quality for delivery to the engine. Low heat leak minimizes tank pressure build-up during vehicle non-operational time periods and prevents venting of fuel during a designed "no vent" standby time.
Disclosure of Invention Technical Problem
[3] LNG is a dynamic fuel exhibiting fluid characteristics that vary with pressure and
corresponding amount of internal energy. These variable fluid characteristics coupled with a cryogenic liquid temperature of -2580F at normal atmospheric pressure necessitate specific equipment and a system design that will enable efficient introduction of LNG into the tank(s) with an effective control of fill level in the tank. Also, the system controls must maintain a specified fuel supply flow rate to a vehicle engine within a specified pressure range during all modes of vehicle operation.
[4] An object of the invention is to effect the fill of the tank, the delivery of liquid from the tank and achieve pressure management of the tank with a single line thus providing a multi- function capability and reducing the number of tank penetrations and therefore a significant reduction in heat transfer.
[5] Another object of the present invention is to provide a reliable means of controlling the ullage space within the tank in order to comply with applicable Federal and State codes in the United States. The vent return line, as employed in the invention, serves as a device that provides an indication of when the tank is filled to the maximum allowable liquid level and will allow for the expansion of the LNG after the fill of the tank. This is accomplished by means of a tubular elbow welded to the end of the vent line serpentine tube in the interior of the tank, in a position perpendicular to the liquid surface of the LNG. With the entrant tube housing assembly installed in the upper part of the tank head it is possible to establish the exact elevation of this elbow above the liquid level and thereby provide a flow path for the liquid out of the tank while at the same time establishing a pressure pad at the top of the tank that prevents the tank from being overfilled.
[6] An object fulfilled by the invention is that, due to improved thermal protection design, "liquid only" can be delivered from the tank, thus assuring consistent fuel quality and pressure from the tank to an external heat exchanger for vaporization and delivery to an engine.
[7] Another object of the present invention is to provide for the reliable installation of a capacitance gauge probe in combination with the liquid fill/withdrawal tube. The capacitance probe is attached to the entrant tube unit by fittings welded to the vertical portion of the fill/withdrawal tubing.
[8] The filling, venting, pressure management and flow control assembly and system provided by this invention will satisfy applicable codes for maximum allowable tank fill level as well as the fuel pressure and flow rate requirements of any vehicle engine. Technical Solution
[9] As shown in Figs. 1 and 2, a conduit assembly includes a pair of tubes 10, 12 that extend through an end wall of a tank 13 for a cryogenic liquid. A tank to which the conduit assembly is applicable is disclosed in U.S. Patent No. 6,880,719 Bl. The tank
makes use of a double wall construction having an inner shell 14 that holds the liquid under pressure and an outer shell 16 that surrounds the inner shell and is spaced from it. A barrier to heat transfer into the inner shell is provided by an evacuated space 18 between the inner and outer shells.
[10] As shown, the tubes have a serpentine form and extend side-by-side horizontally within an upper region of the inner shell. As best shown in Fig. 1, the tubes extend through outer and inner housings 20, 22 forming an extension of the evacuated space between the inner and outer shells. In particular, the tubes extend through a closure plate 20a on the outer housing, through the evacuated space between the shells, through the inner housing and closure plate 22a and into an upper central region of the inner shell.
[11] One of the tubes 10, used for filling and withdrawal of liquid, includes a vertical section 10a that extends toward the bottom of the inner shell and has an opening at its lower end, Located adjacent to the vertical section 10a of tube 10 is a liquid level capacitance gauge 24.
[12] The other tube 12, used for venting and fill level control, terminates in the upper central region of the inner shell at an elbow 12a with a downwardly facing opening 12b. An electrical lead 24a from the capacitance gauge 24 is shown extending through the vent tube.
[13] A cryogenic liquid from a bulk supply flowing through the fill tube enters the inner shell at the bottom. As the liquid level rises, gases above the surface of the liquid can flow from the inner shell through the vent tube 12 and back to the bulk supply. When the liquid level rises to immerse the bottom of the elbow 12b, liquid will flow through the vent tube back to the bulk supply. A gas pressure pad established above the surface of the liquid will prevent further rise of the liquid in the inner shell. The elbow 12a is located so that the downwardly facing opening is generally coincident with the fill level mandated by applicable codes. The position of the elbow also establishes the proper "ullage space" (tank space not occupied by liquid) in the container, to allow for expansion of the LNG after filling.
[14] Figs. 3 and 4 show a preferred embodiment of a system for effecting flow control and pressure management of a cryogenic liquid held in a tank. An elbow 12a of third conduit 30 is coupled to the outer end of fill and withdrawal conduit 10 that communicates with the bottom of tank 13. The other end of third conduit 30 is coupled to an outer end of tank vent tube 12 via a passage in manifold 32. A pressure regulator 34 is disposed in third conduit 30 between its couplings with conduits 10 and 12. Thus, third conduit 30 forms a loop between fill and withdrawal conduit 10 and vent tube 12, and the pressure regulator 34 is interposed in the loop. The pressure regulator incorporates a normally closed valve that opens in response to a drop in pressure in third
conduit 30 below a predetermined level. A pressure regulator found to be suitable for this application is RegO Products Part No. RG 125.
[15] Fourth conduit 36 for conducting vapor from the tank to a bulk supply is coupled to third conduit 30 via a passage in the manifold 32 a shut off valve 38 (normally open) is disposed in fourth conduit 36. Also, coupled to the manifold are primary and secondary relief valves 40, 42. Teed into third conduit 30 between the coupling with conduit 10 and the pressure regulator 34 are fifth conduit 44 which receives cryogenic liquid from a bulk supply (not shown), and sixth conduit 46 which conducts cryogenic liquid to a point of use, such as a vehicle engine (not shown). As shown, an accumulator 48 and a check valve 50 are also disposed in third conduit 30 between the regulator 34 and the coupling with sixth conduit 46. A shut-off valve 52 (normally open) is disposed in third conduit 30 between the couplings with fill and withdrawal conduits 10 and fifth conduit 44. A solenoid valve 54 is disposed in sixth conduit 46 to allow or block flow of liquid to a point of use.
[16] The regulator 34 will maintain a constant delivery pressure to an engine. When liquid is being provided to an engine, the liquid level in the tank will fall and the pressure in third conduit 30 may also fall. When the pressure in the third conduit 30 falls below a predetermined level, the valve in the regulator 34 will open, liquid in the accumulator 48 will pass through check valve 50 and regulator 34 and into the third conduit 30 on the other side of the regulator. This section third of conduit 30 acts as a heat exchanger in which liquid in the conduit will be vaporized by heat from ambient, causing expansion of the fluid in the conduit which causes a pressure build. In practice, very small amounts of liquid passing through the check valve 50 and the regulator 34 effect a pressure build that returns the pressure in conduit to a required level. When the pressure reaches the predetermined level, the regulator shuts off, stopping vaporization and pressure build-up. As liquid is forced from the tank, pressure in the tank begins to drop and the pressure build regulator again begins operating.
[17] In some cases, where the LNG saturation pressure is above the minimum tank operating pressure, the pressure build system, just described, will never be activated at any flow rate of fuel from the tank. Minimum pressure is controlled by the liquid saturation pressure. However, when liquid saturation pressure is below the specified minimum tank operating pressure, or in any case where pressure has decayed at low tank quantity with high flow rates, the pressure build system will maintain pressure within the required operating range.
[18] Excessive pressures in third conduit 30 are relieved by the opening of primary and/ or secondary relief valves 40, 42.
Claims
[1] In combination, a tank for holding a cryogenic liquid and a conduit assembly, wherein: the tank comprises an inner shell 14 for holding a cryogenic liquid, an outer shell 16 surrounding the inner shell 14 and an evacuated space between the inner shell 14 and the outer shell 16; the conduit assembly includes (1) a fill and withdrawal conduit 10 for conducting flow of cryogenic liquid into and out of the tank and (2) a vent tube 12 for discharging the air of the inner shell and fill level control in the inner shell; the first conduit includes (1) an extension extending generally horizontally through adjacent walls of both the inner shell 14 and the outer shell 16, through the evacuated space and within an upper region of the inner shell and (2) a vertical section 10a joined to an elbow 12a of the extension and extending downwardly within the inner shell toward the bottom of the inner shell and (3) an opening 12b located near the bottom of the inner shell; and the vent tube 12 includes (1) an extension extending generally horizontally through adjacent walls of both the inner shell 14 and the outer shell 16, through the evacuated space and within an upper region of the inner shell and (2) an elbow 12a with a downwardly facing opening 12b located in an upper region of the inner shell.
[2] The combination as recited in claim 1, wherein: the inner shell includes a housing extending generally horizontally within an upper region of the inner shell, the housing forming an extension of the evacuated space and having a closure plate 20a in an upper central region of the inner shell; and the extensions of the fill and withdrawal conduit 10 and the vent tube 12 extend through the housing and through the closure plate 20a into the interior of the inner shell 14.
[3] The combination as recited in claim 1 or claim 2, wherein at least portions of the extensions of the fill and withdrawal conduit 10 and the vent tube 12 are configured as serpentine tubes that extend alongside each other.
[4] The combination as recited in claim 1 or claim 2, and further comprising a liquid level capacitance gauge within the inner shell 14 adjacent to the vertical section 10a of the fill and withdrawal conduit 10.
[5] The combination as recited in claim 3, and further comprising a liquid level capacitance gauge within the inner shell 14 adjacent to the vertical section 10a of the fill and withdrawal conduit 10.
[6] A system for effecting flow control and pressure management of a cryogenic liquid held in a tank, the system comprising: a fill and withdrawal conduit 10 communicating with the interior of the tank near the bottom of the tank; a vent tube 12 communicating with the interior of the tank at an upper region of the tank; a third conduit 30 communicating with the fill and withdrawal conduit 10 and the vent tube 12 and extending between the fill and withdrawal conduit 10 and vent tube 12 outside of the tank; a pressure regulator disposed in the third conduit 30, the pressure regulator comprising a normally closed valve that opens in response to a pressure drop in the third conduit 30 below a predetermined level; a check valve 50 disposed in the third conduit 30 between the fill and withdrawal conduit 10 and the pressure regulator; a fourth conduit for conducting vapor from the tank to a bulk supply, the fourth conduit being joined to the third conduit 30 between the vent tube 12 and the pressure regulator; a fifth conduit 44 for introducing cryogenic liquid from a bulk supply to the tank, the fourth conduit communicating with the third conduit 30 between the fill and withdrawal conduit 10 and the check valve 50; and a sixth conduit 46 for conducting cryogenic liquid to a point of use, the fifth conduit being joined to the third conduit 30 between the fill and withdrawal conduit 10 and the check valve 50. [7] The system as recited in claim 6, and further comprising a reservoir for holding cryogenic liquid in the third conduit 30, the reservoir being located in the third conduit 30 adjacent to the check valve 50 and between (1) the fifth conduit 44 and the sixth conduit 46 and (2) the check valve 50. [8] The system as recited in claim 6 or claim 7, and further comprising: a shut off valve 38 (normally open) in the fourth 36 conduit for allowing or blocking flow of vapor through the fourth conduit 36 between the tank and a bulk supply; and a solenoid valve 54 for allowing or blocking flow of cryogenic liquid through the third conduit 30 and the fourth conduit 36 between a bulk supply and the fill and withdrawal conduit 10. [9] The system as recited in claim 6 or claim 7, and further comprising a solenoid valve 54 in the sixth conduit 46 for allowing or blocking flow of cryogenic liquid through the sixth conduit 46 between the third conduit 30 and a point of use. [10] The system as recited in claim 8, and further comprising a solenoid valve 54 in
the sixth conduit 46 for allowing or blocking flow of cryogenic liquid through the sixth conduit 46 between the third conduit 30 and a point of use.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR10-2007-0003780 | 2007-01-12 | ||
KR1020070003780A KR100844223B1 (en) | 2007-01-12 | 2007-01-12 | Tank for holding a cryogenic liquid and a conduit assembly, and a system for effecting flow control and pressure management of a cryogenic liquid held in the tank |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2008085005A1 true WO2008085005A1 (en) | 2008-07-17 |
Family
ID=39608846
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/KR2008/000185 WO2008085005A1 (en) | 2007-01-12 | 2008-01-11 | Tank for holding a cryogenic liquid and a conduit assembly, and a system for effecting flow control and pressure management of a cryogenic liquid held in the tank |
Country Status (2)
Country | Link |
---|---|
KR (1) | KR100844223B1 (en) |
WO (1) | WO2008085005A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120000209A1 (en) * | 2008-11-04 | 2012-01-05 | Cryogenic Fuels Inc. | Assembly and system for tank filling, withdrawal and pressure management of a cryogenic liquid |
WO2015012883A1 (en) * | 2013-07-23 | 2015-01-29 | Neill Brendan | Storage and delivery system for a liquid cryogen |
KR101655906B1 (en) * | 2015-06-08 | 2016-09-09 | 한국과학기술연구원 | Cryogenic effective thermal conductivity tester of insulation material |
CN109681772A (en) * | 2018-11-22 | 2019-04-26 | 天津市振津石油天然气工程有限公司 | A kind of LNG liquefaction plant is pressurized liquid device with skid |
EP3755940A4 (en) * | 2018-01-19 | 2021-12-22 | Cryo - Science Sp. Z O.O. | Head for a storage container for liquids |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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EP2788215B1 (en) | 2011-12-07 | 2020-01-15 | Agility Fuel Systems LLC | Systems and methods for monitoring and controlling fuel systems |
CN105318939A (en) * | 2014-08-05 | 2016-02-10 | 重庆巨创计量设备股份有限公司 | LNG dispenser calibrating device |
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JPH08128595A (en) * | 1994-09-09 | 1996-05-21 | Daido Hoxan Inc | Low temperature liquefied gas storage tank |
JP2006057787A (en) * | 2004-08-23 | 2006-03-02 | Iwatani Industrial Gases Corp | Liquefied gas tank and liquefied gas filling method into tank |
JP2006200563A (en) * | 2005-01-18 | 2006-08-03 | Toyota Motor Corp | Liquid fuel supply system |
-
2007
- 2007-01-12 KR KR1020070003780A patent/KR100844223B1/en not_active IP Right Cessation
-
2008
- 2008-01-11 WO PCT/KR2008/000185 patent/WO2008085005A1/en active Application Filing
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH08128595A (en) * | 1994-09-09 | 1996-05-21 | Daido Hoxan Inc | Low temperature liquefied gas storage tank |
JP2006057787A (en) * | 2004-08-23 | 2006-03-02 | Iwatani Industrial Gases Corp | Liquefied gas tank and liquefied gas filling method into tank |
JP2006200563A (en) * | 2005-01-18 | 2006-08-03 | Toyota Motor Corp | Liquid fuel supply system |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120000209A1 (en) * | 2008-11-04 | 2012-01-05 | Cryogenic Fuels Inc. | Assembly and system for tank filling, withdrawal and pressure management of a cryogenic liquid |
US8403000B2 (en) | 2008-11-04 | 2013-03-26 | Cryogenic Fuels, Inc. | Assembly and system for tank filling, withdrawal and pressure management of a cryogenic liquid |
WO2015012883A1 (en) * | 2013-07-23 | 2015-01-29 | Neill Brendan | Storage and delivery system for a liquid cryogen |
KR101655906B1 (en) * | 2015-06-08 | 2016-09-09 | 한국과학기술연구원 | Cryogenic effective thermal conductivity tester of insulation material |
EP3755940A4 (en) * | 2018-01-19 | 2021-12-22 | Cryo - Science Sp. Z O.O. | Head for a storage container for liquids |
CN109681772A (en) * | 2018-11-22 | 2019-04-26 | 天津市振津石油天然气工程有限公司 | A kind of LNG liquefaction plant is pressurized liquid device with skid |
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