EP2288811A2 - Device and method for pumping a cryogenic fluid - Google Patents
Device and method for pumping a cryogenic fluidInfo
- Publication number
- EP2288811A2 EP2288811A2 EP09761888A EP09761888A EP2288811A2 EP 2288811 A2 EP2288811 A2 EP 2288811A2 EP 09761888 A EP09761888 A EP 09761888A EP 09761888 A EP09761888 A EP 09761888A EP 2288811 A2 EP2288811 A2 EP 2288811A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- pump
- pressure
- reservoir
- tank
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000012530 fluid Substances 0.000 title claims abstract description 51
- 238000005086 pumping Methods 0.000 title claims abstract description 21
- 238000000034 method Methods 0.000 title claims description 11
- 239000007788 liquid Substances 0.000 claims abstract description 21
- 238000001816 cooling Methods 0.000 claims description 15
- 239000003638 chemical reducing agent Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 42
- 239000001257 hydrogen Substances 0.000 description 35
- 229910052739 hydrogen Inorganic materials 0.000 description 35
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 33
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 150000002431 hydrogen Chemical class 0.000 description 4
- 238000009434 installation Methods 0.000 description 4
- 238000007872 degassing Methods 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000002955 isolation Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000013517 stratification Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B15/00—Pumps adapted to handle specific fluids, e.g. by selection of specific materials for pumps or pump parts
- F04B15/06—Pumps adapted to handle specific fluids, e.g. by selection of specific materials for pumps or pump parts for liquids near their boiling point, e.g. under subnormal pressure
- F04B15/08—Pumps adapted to handle specific fluids, e.g. by selection of specific materials for pumps or pump parts for liquids near their boiling point, e.g. under subnormal pressure the liquids having low boiling points
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B23/00—Pumping installations or systems
- F04B23/02—Pumping installations or systems having reservoirs
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
- F04B2205/00—Fluid parameters
- F04B2205/01—Pressure before the pump inlet
Definitions
- the present invention relates to a device and a method for pumping a cryogenic fluid.
- the invention relates more particularly to a device for pumping a cryogenic fluid, comprising a storage tank for a cryogenic fluid containing cryogenic liquid, a cryogenic pump having a loss (NPSH) of input charge, a line of suction connecting the reservoir to the pump, the pumping device comprising a system for controlling the pressure in the reservoir to selectively maintain the pressure in the reservoir at least equal to the saturation pressure of the stored cryogenic fluid increased by the loss (NPSH) input load of the cryogenic pump and possibly also increased the value of the pressure drops due to the piping of the suction line connecting the tank to the pump.
- NPSH loss loss
- the invention finds a particularly advantageous application in the field of pumping low-density cryogenic fluids comprising gases such as hydrogen or helium, as well as their isotopes.
- a liquid hydrogen pump (LH2) at 700 bar has a pressure drop "NPSH" of about 250 mbar, which corresponds to a liquid hydrogen height of 35 m. It is impossible to operate the pump with a source tank installed on the pump at a height of 35m (even if it was industrially possible, the pressure losses in lines would compensate for the installation in charge of the tank). A solution is therefore to "cool" the liquid and suck this liquid under cooling. Subcooling is the process of increasing the pressure of a saturated fluid, or of reducing its temperature, at constant pressure, without waiting for the establishment of a new liquid-vapor equilibrium.
- Hydrogen under pressure is however less dense than hydrogen at atmospheric pressure.
- the density of saturated hydrogen at 1 bar absolute is 70 g / l while it is 56g / l at 7 bar absolute. Since liquid hydrogen pumps are volumetric systems, it is therefore interesting to suck up the densest possible hydrogen, thus saturated at the lowest possible pressure (the coldest), in order to optimize the quantities pumped.
- the invention described below makes it possible in particular to use a plant for pumping liquid hydrogen continuously from a source of hydrogen in liquid-gas equilibrium at a low pressure (between 1 and 12 bar) and optimize the operation of such an installation by allowing continuous operation of the pump while maximizing the density of the pumped hydrogen, thus maximizing the pumped flow rate.
- the tank is pressurized via a thermosyphon (atmospheric pressure warmer), or directly by high pressure hydrogen in bottles at room temperature.
- thermosyphon atmospheric pressure warmer
- high pressure hydrogen in bottles at room temperature.
- the device according to the invention is essentially characterized in that the pressure control system comprises at least one of: pipe connecting a high pressure outlet of the pump to the reservoir for selectively injecting pumped cold fluid into the reservoir, a pipe connecting a source of high pressure gas to the reservoir via a gas cooling member, for selectively injecting cooled gas into the reservoir .
- the pressure control system comprises a pipe connecting a high pressure outlet of the pump to the reservoir to reinject pumped fluid into the reservoir during the operation of the pump, and a pipe connecting a source of high pressure gas to the tank via a cooling member, for injecting cooled gas into the tank, especially when the pump is inactive,
- the pipe connecting a high-pressure outlet of the pump to the tank comprises an expander for reinjecting cold gas into the tank
- the cooling element situated in the pipe connecting the source of high-pressure gas to the tank comprises a heat exchanger able to selectively heat-exchange the gas coming from the source of high-pressure gas with the cryogenic fluid pumped from the tank;
- the heat exchanger comprises a cold accumulator for maintaining cooling power by thermal inertia between two uses of the pump, the source of high pressure gas is connected to a high pressure outlet of the pump via at least one among: a valve, an expansion valve, a heater, to allow the selective filling of said source with fluid from the reservoir,
- the device comprises a gas evacuation line generated by the operation of the pump, said gas evacuation line connecting a gas outlet of the pump to the tank or to a separate degassing storage,
- the cold accumulator comprises at least one of: an aluminum mass, a brine, copper or lead-based alloy mass, -
- the heat exchanger accumulator of the heat exchanger has a mass heat capacity (density * Heat capacity at constant pressure) of between 1400 and 4000 kJ.m-3.K-1 and a thermal conductivity of between 30 and 400 W / mK, -
- the pressure control system comprises a pressure sensor and a temperature sensor of the cryogenic fluid in the tank and / or in the suction line, connected to a calculation and control logic for providing the signals measured to control the injection of fluid into the reservoir from the pump (3) (via line 9) and / or from the source (16) of high pressure gas (via line 10, 9),
- the device comprises a gas supply line having an end connectable to a user and an end connected to a high pressure outlet of the pump via at least one heater and a pressure regulator,
- the pressure control system comprises at least one calculation and control block capable of calculating, from the temperature measured by said temperature sensor, a minimum value of the pressure measured by said pressure sensor equaling the saturation pressure; of the liquid said temperature increased by the loss (NPSH) of the inlet charge of the pump and any pressure losses in the piping in the suction line, - the reservoir is filled with cryogenic fluid saturated with its vapor, the fluid cryogenic is preferably a low density fluid such as hydrogen or helium,
- the invention also relates to a method of pumping a cryogenic fluid from a cryogenic fluid reservoir comprising cryogenic liquid, the fluid being pumped via a suction line comprising a cryogenic pump having an inlet pressure drop, the method comprising a step of controlling the pressure in the reservoir to selectively maintain the pressure in the reservoir and / or in the suction line at least equal to the saturation pressure of the cryogenic fluid increased by the inlet pressure drop of the cryogenic pump and possibly also increased the value of the pressure drops due to the piping of the suction line connecting the tank to the pump.
- the method is characterized in that the step of controlling the pressure in the tank comprises introducing said cold gas into the tank at a temperature below room temperature outside the tank and preferably between between 40 0 K and 100 0 K and at a pressure between 1 and 12 bar.
- the step of controlling the pressure in the tank comprises introducing said cold gas into the tank at a temperature below room temperature outside the tank and preferably between between 40 0 K and 100 0 K and at a pressure between 1 and 12 bar.
- the cold gas introduced into the tank for controlling the pressure in the tank is supplied by at least one of: a pipe connecting a high pressure outlet of the pump to the tank, a pipe connecting a source of high pressure gas to the tank via a gas cooling member,
- the introduction of cold gas into the tank is selectively provided by a pipe connecting a high pressure outlet of the pump to the tank when the pump is in operation and a pipe connecting a source of high pressure gas to the tank via a cooling member gas when the pump is stopped,
- the cold gas supplied by the pipe connecting a high-pressure outlet of the pump to the tank is obtained by expansion of the fluid coming from the high-pressure outlet of the pump, and in that the cooling member of the gas coming from the source of High pressure gas uses frigories of the fluid pumped from the tank.
- the invention may also relate to any alternative device or method comprising any combination of the above or below features.
- FIG. 1 represents a schematic view illustrating the structure and operation of a device for pumping a cryogenic fluid according to a first embodiment of the invention
- FIG. 2 shows a schematic view illustrating the structure and operation of a device for pumping a cryogenic fluid according to a second embodiment of the invention.
- the device comprises a reservoir
- cryogenic fluid isolated under vacuum
- a liquid-gas mixture for example at the temperature and a pressure of between 1 and 12 bar abs.
- the temperature and the pressure in the tank 1 are measured by sensors
- the lower part of the tank 1 is connected to the suction inlet of a cryogenic pump 3 by a suction line 2 vacuum insulated and comprising one or more isolation valves.
- the pump 3 comprises a gas evacuation line 4 (produced for example by heating / friction) towards the upper part of the tank 1 and provided with valves.
- the pump is connected to a high pressure discharge line 5 generally incorporating a discharge valve (high pressure outlet of the pumped fluid).
- the high-pressure discharge line 5 is connected to a cold hydrogen feed line 6 of a preferably high-inertia exchanger 10.
- the fluid passes through a cold high-pressure line 11 and then through a high-pressure atmospheric heater (or equivalent) 12 to a gas supply line 111 having an end connectable to a user U (tank or bottle for example) via a pressure regulator 13.
- the thermally isolated high-pressure discharge line 5 is also connected to the upper part of the tank 1 via a pipe 9 for pressurizing the tank 1 by cooled hydrogen coming from the pump 3.
- the pipe 9 for pressurizing the tank 1 comprises a pressure reducer 99 and / or a control valve.
- the upper end of the tank 1 is connected to a valve 20 for depressurizing the tank (towards the outside), for example via the pressurization pipe 9.
- the pressurization pipe 9 is also connected to a source 16 of pressurized gas such as bottles 16 at ambient temperature via a line 29 passing through the exchanger 10 with high inertia (with heat exchange) and comprising a control valve 15 ( regulator for example).
- a source 16 of pressurized gas such as bottles 16 at ambient temperature via a line 29 passing through the exchanger 10 with high inertia (with heat exchange) and comprising a control valve 15 ( regulator for example).
- the gas supply line 111 is also connected to the source 6 of high-pressure gas via a pressure reducer 14.
- a block 18 for controlling the pressure of the tank 1 receives the pressure information from the pressure sensor 100 and controls a selector 17 which selectively actuates the pressure reducer / control valve 99 of the pressurization pipe 9 and the valve 15. control of the line 29 connected to the source 16 of gas under pressure.
- a calculation block 19 determines the saturation pressure in the tank 1 as a function of the temperature detected by the valve 101 and controls the control block 19 according to the result.
- the hydrogen at the pressure, and the temperature of the tank 1 is supplied by the tank 1 to the pump 3 via the isolated line 2 under vacuum.
- the hydrogen is pumped by the pump 3 and is discharged at high pressure (between 200 and 850 bar for example) by the discharge line 5 to the exchanger 10 and the line 11 high cold pressure.
- Heater 12 increases the temperature of hydrogen to room temperature.
- the expander 14 ensures that the reservoirs 16 are at a maximum pressure.
- the upstream pressure regulator 13 controls the pressure in the pump.
- the system carries out a control of the pressure of the tank 1.
- the set pressure of the tank 1 is calculated by the calculation block 19 so that the pressure in the tank is equal to the saturation pressure of the hydrogen at the raised temperature (101) plus the loss
- NPSH pressure drop
- the device according to the invention has the possibility of using, during the operation of the pump 3, hydrogen coming directly from the cold high pressure outlet 5 of the pump 3 (for example hydrogen at approximately 70 ° K. for 450 bar pressure).
- This hydrogen supplied by the pump 3 can be expanded via the valve 99 of the pressurization pipe 9 and reinjected into the tank 1 in the form of gas and / or cold liquid.
- the device according to the invention furthermore has the possibility of using, before starting the pump 3, high-pressure bottles 16 at ambient temperature to inject cold hydrogen (by passing through the exchanger / accumulator 10) in the tank 1 in order to cool the hydrogen by pressurizing the tank 1.
- the cold accumulator (in the exchanger 10) is for example previously cold set during the operation preceding the pump 3.
- the cold accumulator can be insulated with polyurethane foam or equivalent.
- the tank 1 can be depressurized by means of the depressurization valve 20 of the tank 1, in order to cool the hydrogen remaining in the tank 1.
- the hydrogen used for the pressurization of the tank 1 is thus pre-cooled.
- the thermal stratification of the gas in the tank is then lower, its rise in pressure is slower, which increases the pumping time available before reaching the maximum operating pressure of the tank 1.
- the heat exchanger 10 to high inertia and preferably isolated from the outside makes it possible to have a source of cold which makes it possible to pressurize the tank 1 with cold hydrogen even when the pump 3 is not in use (from bottles 16 or equivalent).
- Thermal inertia of the exchanger 10 and its isolation mode is determined so that its temperature preferably remains constant (+/- 10 0 C) between two phases of operation of the pump 3.
- the device described allows a greater accuracy and speed of control of the pressure of the tank 1 than in the prior art, especially with respect to a thermosiphon system.
- FIG. 1 illustrates a variant which differs from the embodiment of Figure 1 only with respect to the line 4 of gas evacuation.
- the other elements are designated by the same references and are not described a second time.
- the line 4 for evacuating or returning hydrogen is returned to a so-called degassing capacity 21.
- the return line 4 communicates with a degassing tank 21 whose level is controlled by valves 23, 24 after having been heated by an atmospheric heater 22. This configuration makes it possible to prevent the hot hydrogen from returning to the atmosphere. the cryogenic tank 1 and warms all the liquid hydrogen contained therein.
- the invention thus makes it possible to obtain an under cooling of the cryogenic fluid and an aspiration of the fluid thus sub-cooled.
- the compensation of the inlet pressure drop is thus achieved, avoiding any cavitation phenomenon in the pump 3 while the fluid is maintained at a pressure sufficiently low to maximize the density of the fluid and therefore the quantity pumped.
- control of the pressurization of the tank 1 according to the invention does not affect or little the level of liquid in the tank and thus pumping time available before reaching the maximum operating pressure of the tank 1.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0853168A FR2931213A1 (en) | 2008-05-16 | 2008-05-16 | DEVICE AND METHOD FOR PUMPING A CRYOGENIC FLUID |
PCT/FR2009/050844 WO2009150337A2 (en) | 2008-05-16 | 2009-05-07 | Device and method for pumping a cryogenic fluid |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2288811A2 true EP2288811A2 (en) | 2011-03-02 |
EP2288811B1 EP2288811B1 (en) | 2012-02-15 |
Family
ID=40083678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09761888A Active EP2288811B1 (en) | 2008-05-16 | 2009-05-07 | Device and method for pumping a cryogenic fluid |
Country Status (7)
Country | Link |
---|---|
US (1) | US9546645B2 (en) |
EP (1) | EP2288811B1 (en) |
JP (1) | JP5313338B2 (en) |
CN (1) | CN102027236B (en) |
AT (1) | ATE545784T1 (en) |
FR (1) | FR2931213A1 (en) |
WO (1) | WO2009150337A2 (en) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8543245B2 (en) * | 2009-11-20 | 2013-09-24 | Halliburton Energy Services, Inc. | Systems and methods for specifying an operational parameter for a pumping system |
US8365551B2 (en) * | 2010-12-09 | 2013-02-05 | General Electric Company | Vacuum insulator for a refrigerator appliance |
US20140190187A1 (en) | 2013-01-07 | 2014-07-10 | Hebeler Corporation | Cryogenic Liquid Conditioning and Delivery System |
JP6438938B2 (en) | 2013-04-22 | 2018-12-19 | チャート・インコーポレイテッドChart Inc. | Liquid natural gas cooling on the fly |
US9347615B2 (en) * | 2013-09-13 | 2016-05-24 | Air Products And Chemicals, Inc. | Low-loss cryogenic fluid supply system and method |
FR3022233B1 (en) * | 2014-06-12 | 2019-06-07 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | DEVICE AND METHOD FOR SUPPLYING FLUID |
US9828987B2 (en) * | 2015-01-30 | 2017-11-28 | Caterpillar Inc. | System and method for priming a pump |
DE102017008210B4 (en) * | 2017-08-31 | 2020-01-16 | Messer France S.A.S. | Device and method for filling a mobile refrigerant tank with a cryogenic refrigerant |
FR3089599B1 (en) * | 2018-12-06 | 2020-11-13 | Air Liquide | Cryogenic fluid storage tank |
FR3089600B1 (en) * | 2018-12-06 | 2021-03-19 | Air Liquide | Cryogenic fluid storage tank |
US20210180751A1 (en) * | 2019-12-16 | 2021-06-17 | Bharat Barney Patel | Portable, cryogenic fluid pump apparatus with associated instrumentation, conduit legs and accessories |
US20230287875A1 (en) * | 2022-03-08 | 2023-09-14 | Air Products And Chemicals, Inc. | Apparatus and method for cryogenic pump cooldown |
Family Cites Families (22)
Publication number | Priority date | Publication date | Assignee | Title |
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US3632235A (en) * | 1969-06-09 | 1972-01-04 | Carl A Grenci | Cryogenic pump system |
FR2439881A1 (en) * | 1978-10-23 | 1980-05-23 | Air Liquide | METHOD AND DEVICE FOR STARTING A CRYOGENIC LIQUID PUMP |
FR2506400B1 (en) * | 1981-05-19 | 1986-03-21 | Air Liquide | METHOD AND PLANT FOR PUMP TRANSFER OF A CRYOGENIC LIQUID |
US5243821A (en) * | 1991-06-24 | 1993-09-14 | Air Products And Chemicals, Inc. | Method and apparatus for delivering a continuous quantity of gas over a wide range of flow rates |
US5360139A (en) * | 1993-01-22 | 1994-11-01 | Hydra Rig, Inc. | Liquified natural gas fueling facility |
FR2707371B1 (en) * | 1993-07-08 | 1995-08-11 | Air Liquide | Installation for supplying gas under high pressure. |
DE19717267B4 (en) * | 1997-04-24 | 2008-08-14 | Alstom | Process for the preparation of refrigerated liquefied gas |
DE10107187A1 (en) * | 2001-02-15 | 2002-08-29 | Linde Ag | Gas station for cryogenic media |
US6474078B2 (en) * | 2001-04-04 | 2002-11-05 | Air Products And Chemicals, Inc. | Pumping system and method for pumping fluids |
US20030213246A1 (en) * | 2002-05-15 | 2003-11-20 | Coll John Gordon | Process and device for controlling the thermal and electrical output of integrated micro combined heat and power generation systems |
JP2003148695A (en) * | 2001-11-12 | 2003-05-21 | Toho Gas Co Ltd | Liquefied natural gas |
US6564579B1 (en) * | 2002-05-13 | 2003-05-20 | Black & Veatch Pritchard Inc. | Method for vaporizing and recovery of natural gas liquids from liquefied natural gas |
US6889508B2 (en) * | 2002-10-02 | 2005-05-10 | The Boc Group, Inc. | High pressure CO2 purification and supply system |
JP4272419B2 (en) * | 2002-12-25 | 2009-06-03 | Ihiプラント建設株式会社 | Method and apparatus for discharging small volume by pump of cryogenic liquid |
FR2855598B1 (en) * | 2003-05-28 | 2005-10-07 | Air Liquide | METHOD AND INSTALLATION FOR SUPPLYING PRESSURE GAS RELIEF BY CRYOGENIC LIQUID VAPORIZATION |
GB0320474D0 (en) * | 2003-09-01 | 2003-10-01 | Cryostar France Sa | Controlled storage of liquefied gases |
US20050076639A1 (en) * | 2003-10-14 | 2005-04-14 | Shirk Mark A. | Cryogenic cogeneration system |
FR2866929B1 (en) * | 2004-03-01 | 2008-04-04 | Air Liquide | SYSTEM FOR PUMPING A CRYOGENIC FLUID |
US8499569B2 (en) * | 2004-09-13 | 2013-08-06 | Argent Marine Management, Inc. | System and process for transporting LNG by non-self-propelled marine LNG carrier |
JP2007024166A (en) * | 2005-07-15 | 2007-02-01 | Taiyo Nippon Sanso Corp | Low-temperature liquefied gas supply device |
FR2891347B1 (en) * | 2005-09-28 | 2007-11-02 | Air Liquide | METHOD AND DEVICE FOR FILLING A PRESSURIZED GAS IN A RESERVOIR |
DE102006019993B3 (en) * | 2006-04-26 | 2007-12-27 | Daimlerchrysler Ag | Compressed gas e.g. hydrogen, storage for e.g. fuel cell vehicle, has cooling device provided for heat transfer medium, where part of gas is supplied as heat transfer medium to cooling device through branching of filling device |
-
2008
- 2008-05-16 FR FR0853168A patent/FR2931213A1/en active Pending
-
2009
- 2009-05-07 WO PCT/FR2009/050844 patent/WO2009150337A2/en active Application Filing
- 2009-05-07 US US12/993,009 patent/US9546645B2/en active Active
- 2009-05-07 CN CN2009801174794A patent/CN102027236B/en active Active
- 2009-05-07 JP JP2011508977A patent/JP5313338B2/en not_active Expired - Fee Related
- 2009-05-07 EP EP09761888A patent/EP2288811B1/en active Active
- 2009-05-07 AT AT09761888T patent/ATE545784T1/en active
Non-Patent Citations (1)
Title |
---|
See references of WO2009150337A2 * |
Also Published As
Publication number | Publication date |
---|---|
EP2288811B1 (en) | 2012-02-15 |
US20110070103A1 (en) | 2011-03-24 |
US9546645B2 (en) | 2017-01-17 |
JP5313338B2 (en) | 2013-10-09 |
WO2009150337A2 (en) | 2009-12-17 |
WO2009150337A3 (en) | 2010-02-18 |
FR2931213A1 (en) | 2009-11-20 |
ATE545784T1 (en) | 2012-03-15 |
CN102027236B (en) | 2013-11-13 |
CN102027236A (en) | 2011-04-20 |
JP2011521180A (en) | 2011-07-21 |
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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 |
|
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