EP3254015A1 - Procédé et un dispositif de remplissage de réservoir d'hydrogène - Google Patents

Procédé et un dispositif de remplissage de réservoir d'hydrogène

Info

Publication number
EP3254015A1
EP3254015A1 EP16707847.6A EP16707847A EP3254015A1 EP 3254015 A1 EP3254015 A1 EP 3254015A1 EP 16707847 A EP16707847 A EP 16707847A EP 3254015 A1 EP3254015 A1 EP 3254015A1
Authority
EP
European Patent Office
Prior art keywords
storage
gas
source
pressure
reservoir
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Withdrawn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
EP16707847.6A
Other languages
German (de)
English (en)
French (fr)
Inventor
Baptiste RAVINEL
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.)
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Publication of EP3254015A1 publication Critical patent/EP3254015A1/fr
Withdrawn legal-status Critical Current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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/002Automated filling apparatus
    • F17C5/007Automated filling apparatus for individual gas tanks or containers, e.g. in vehicles
    • 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/02Special adaptations of indicating, measuring, or monitoring equipment
    • 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • F17C5/04Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases requiring the use of refrigeration, e.g. filling with helium or hydrogen
    • 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
    • F17C5/00Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/06Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed gases
    • 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
    • F17C7/00Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • GPHYSICS
    • G05CONTROLLING; REGULATING
    • G05DSYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
    • G05D23/00Control of temperature
    • G05D23/19Control of temperature characterised by the use of electric means
    • G05D23/20Control of temperature characterised by the use of electric means with sensing elements having variation of electric or magnetic properties with change of temperature
    • G05D23/2033Control of temperature characterised by the use of electric means with sensing elements having variation of electric or magnetic properties with change of temperature details of the sensing element
    • 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
    • F17C2205/0326Valves electrically actuated
    • 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
    • F17C2221/01Pure fluids
    • F17C2221/012Hydrogen
    • 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
    • F17C2223/0107Single phase
    • F17C2223/0123Single 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
    • 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
    • F17C2223/036Very high pressure (>80 bar)
    • 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
    • F17C2225/03Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the pressure level
    • F17C2225/036Very high pressure, i.e. above 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
    • F17C2227/0157Compressors
    • 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
    • F17C2227/0302Heat exchange with the fluid by heating
    • F17C2227/0309Heat exchange with the fluid by heating using another fluid
    • 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
    • F17C2227/0337Heat exchange with the fluid by cooling
    • F17C2227/0341Heat exchange with the fluid by cooling using another fluid
    • 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
    • F17C2227/0372Localisation of heat exchange in or on a vessel in the 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
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/03Control means
    • F17C2250/032Control means using computers
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/043Pressure
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/043Pressure
    • F17C2250/0434Pressure difference
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0486Indicating or measuring characterised by the location
    • F17C2250/0491Parameters measured at or 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/06Controlling or regulating of parameters as output values
    • F17C2250/0605Parameters
    • F17C2250/0626Pressure
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/06Controlling or regulating of parameters as output values
    • F17C2250/0605Parameters
    • F17C2250/0631Temperature
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/06Controlling or regulating of parameters as output values
    • F17C2250/0605Parameters
    • F17C2250/0636Flow or movement of content
    • 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/07Actions triggered by measured parameters
    • F17C2250/072Action when predefined value is reached
    • 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
    • F17C2260/00Purposes of gas storage and gas handling
    • F17C2260/02Improving properties related to fluid or fluid transfer
    • F17C2260/025Reducing transfer time
    • 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
    • F17C2265/06Fluid distribution
    • F17C2265/065Fluid distribution for refuelling vehicle fuel tanks
    • 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
    • F17C2270/0139Fuel stations
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P90/00Enabling technologies with a potential contribution to greenhouse gas [GHG] emissions mitigation
    • Y02P90/45Hydrogen technologies in production processes

Definitions

  • the present invention relates to a method and a device for filling a hydrogen tank.
  • the invention relates more particularly to a method of filling a hydrogen gas tank under pressure from at least one source storage containing hydrogen gas under pressure at a first predetermined temperature and at a predetermined pressure greater than pressure in the tank to be filled, wherein hydrogen is transferred from the source storage to the tank by pressure equalization via a filling circuit having an upstream end connected to the source storage and a downstream end connected to the tank, and wherein, the at least one source storage is in heat exchange with a gas heating member stored in the source storage.
  • the filling of fuel tanks with hydrogen gas is generally carried out via one and preferably several pressure balances between one or more source storages and the reservoir to be filled.
  • a well-known solution uses several source storages connected in parallel and which are used successively to maximize the pressure differences between the source and the reservoir to be filled (“cascading" filling).
  • a compressor may also be provided in addition to supplement or complete the filling if necessary.
  • EP2175187A2 describes a filling system in which the temperature of the gas is controlled (lowered) before entering the tank.
  • the document WO201 1026551 A1 describes a filling system in which the temperature of the source storage is maintained at a determined low level.
  • An object of the present invention is to improve the filling efficiency and / or to overcome all or part of the disadvantages of the prior art noted above.
  • the filling method according to the invention which moreover conforms to the generic definition given in the preamble above, is essentially characterized in that during at least a part of the hydrogen transfer of the source storage to the reservoir, the gas contained in the source storage is heated to a second predetermined temperature which is higher than the first temperature.
  • the at least one storage source is reheated to increase the pressure of the gas in the storage so as to increase the pressure differential compared to the tank to fill.
  • this reheating is carried out when the pressure in the source storage falls below a determined low threshold and / or when the pressure in the reservoir during filling reaches a determined high threshold.
  • embodiments of the invention may include one or more of the following features:
  • the heating of the gas contained in the source storage increases its temperature by a determined value of between 10 ° C. and 60 ° C. and preferably between 20 ° C. and 40 ° C.,
  • the gas contained in the source storage is heated via the reheating member
  • the gas contained in the source storage is reheated only when the pressure differential between the gas in the source storage and, on the one hand, on the other hand, the gas in the reservoir is less than said determined first differential,
  • the first differential determined is between 50 and 250 bar and preferably between 100 and 200 bar
  • the cooling of the gas contained in the source storage decreases its temperature from 10 ° C. to 60 ° C. and preferably from 20 ° C. to 40 ° C.
  • the gas in the source storage has an initial pressure before filling and before reheating of between 150 and 950 bar and in particular between 250 and 850 bar,
  • the invention also relates to a device for filling a pressurized hydrogen gas tank comprising at least one source storage containing hydrogen gas under pressure at a first predetermined temperature and at a predetermined pressure, a gas heating member. stored in the source storage, a filling circuit having an upstream end connected to the source storage and a downstream end removably connectable to the tank to be filled, at least one regulating member of the pressure and / or the flow of gas admitted to circulate in the circuit from the source storage to the tank, an electronic data acquisition, storage and processing member connected to the regulating member, also connected to the gas heating member stored in the source storage and to a pressure sensor in the tank, the electronic data acquisition, storage and processing element being configured for controlling the rate and / or pressure of the gas in the filling circuit, the electronic data acquisition, storage and processing member being configured to control the heating of the gas contained in the source storage at a second predetermined temperature which is greater than the first temperature during at least a portion of the hydrogen transfer from the source storage to the reservoir.
  • the source storage containing
  • 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 and partial view illustrating an example of a filling device that can implement the invention
  • FIG. 2 represents comparative curves of variation of the pressure within source storages and reservoirs during refilling with and without the implementation of the invention.
  • Figure 1 shows schematically and partially an example of filling station 1 tanks of hydrogen gas under pressure (eg vehicle tanks).
  • the station conventionally comprises at least one source storage 2 containing hydrogen gas under pressure, for example at a pressure of between 150 bar and 1000 bar, in particular 700 to 900 bar.
  • the storage sources 2 are for example at room temperature or maintained at a predetermined temperature (for example at 15 ° C or 0 ° C).
  • the station further comprises a filling circuit 3 having an upstream end connected to the storage (s) 2 source and a downstream end removably connectable to the tank 1 to fill.
  • the filling circuit 3 comprises, for example, an isolation valve 4 and a device 5 for regulating the pressure and / or the flow of gas admitted to circulate in the circuit 3 from the source storage 2 to the tank 1.
  • the regulating member 5 comprises for example a valve, controlled or not, a pressure regulator or any other appropriate member for controlling the gas flow or the pressure rise in the tank 1 to be filled.
  • the station further comprises a pressure sensor 8 in the reservoir, located for example in the filling circuit 3 upstream of the tank 1.
  • this sensor 8 can be replaced or supplemented by a pressure sensor in the tank 1, around the tank and / or by software modeling calculating this pressure.
  • the filling circuit 3 may further comprise a heat exchanger 9 in heat exchange with the gas downstream of the member 5 to optionally regulate the temperature of the gas (to cool the gas in particular).
  • the station preferably further comprises an electronic data acquisition, storage and processing member 7, for example a PLC, a computer, a computer or any other microprocessor device or the like.
  • an electronic data acquisition, storage and processing member 7 for example a PLC, a computer, a computer or any other microprocessor device or the like.
  • the electronic device 7 for acquisition, storage and data processing is connected to the regulating member 5 and the gas reheating member 6 stored in the source storage 2 to control / control.
  • the electronic member 7 for storage acquisition and data processing is connected to the sensor 8 of the pressure in the tank 1 to collect the signal of the latter.
  • the electronic device 7 for acquiring, storing and processing data can also be connected to a sensor for measuring the pressure and / or the temperature in the source storage 2 or at its outlet.
  • the station further comprises a member 6 for heating the gas stored in the storage 2 source.
  • the electronic device 7 for acquiring, storing and processing data is configured to control the flow rate and / or the pressure of the gas in the filling circuit so as to optimize the filling (determined time, quantity transferred, without generate a temperature rise above a prescribed threshold, for example determined by the nature of the tank 1).
  • the electronic device 7 for acquiring, storing and processing data is also configured to control the heating of the gas contained in the source storage 2 at a determined temperature which is greater than the current temperature for at least part of the hydrogen transfer from the source storage 2 to the tank 1.
  • this heating is carried out at the end of the transfer of gas between the source storage 2 and the tank 1.
  • the gas contained in the source storage 2 is heated via the reheating member 6.
  • this reheating is performed only when the pressure differential between the gas in the source storage 2 on the one hand and the gas in the reservoir 1 on the other hand is lower than said determined first differential.
  • This first differential determined is for example between 50 and 250 bar and preferably between 100 and 200 bar.
  • the heating of the gas contained in the source storage 2 may be provided to increase its temperature by a determined value, for example between 10 ° C. and 60 ° C. and preferably between 20 ° C. and 40 ° C., in particular 30 ° C.
  • This reheating makes it possible to increase the pressure of the gas in the source storage 2 and thus makes it possible to maximize the pressure differential between the source 2 and the receiver tank 1.
  • the pressure differential can be increased, maintained or, failing that, its decrease can be minimized as long as possible to improve the filling efficiency.
  • the final pressure in the source storage 2 (when warmed up) will be lower than that obtained in the processes of the prior art (without warming). That is to say that the tank 1 will be better filled (better filling efficiency for a given time) and the source storage 2 will be better used (better emptied).
  • the gas can be cooled (for example via an exchanger 9 downstream of the regulating member 5 and / or via a heat exchange directly at the storage 2 source).
  • This well-known cooling helps to minimize heating in the tank 1, especially at the beginning of filling when the expansion of the hydrogen produces a heating surplus effect Joule Thomson in addition to the compression effect
  • the tank 1 At the end of filling the tank 1 can tolerate a relatively hotter gas.
  • the invention is particularly advantageous in the case where a compressor is used in the filling station because the need to use the compressor can be reduced.
  • heating of a coolant for cooling the gas can optionally be used to heat the storage 2 source.
  • the method is particularly advantageous for relatively long fills that is to say having durations of between ten minutes and sixty minutes.
  • the method can also be applied to fast fills (between two and ten minutes for example).
  • FIG. 2 schematically illustrates the effects of the invention with respect to the prior art.
  • the curves in long and short discontinuous lines represent the pressure variation in the filled tank respectively without and with the reheating according to the invention.
  • the source storage gas is cooled or no thermal action is performed on it. It may for example have been pre-cooled at a temperature of -30 ° C for example.
  • the filling is initiated, the pressure in the source storage 2 decreases and that in the target tank 1 increases.
  • the Gas heating in the storage 2 source can be realized.
  • the reheating may consist in achieving an increase of + 30 ° C with respect to the initial temperature, see with respect to the ambient temperature.
  • the gas can be heated up to 70 ° C for example.
  • the inventors are furthermore demonstrated that the solution described above can have advantages in terms of energy balance.
  • reheating can reduce the use of a compressor.
  • the economic balance is positive when the duration of use of a compressor reaches a certain value (for example 120 seconds).
  • the cooling block 9 can be recovered.
  • other heat sources can be used within the filling station (compressors ).
  • the invention makes it possible to insert 0.3 kg of hydrogen in addition to the previous solution without reheating. This corresponds to approximately 25 to 30 seconds of compressor operation saved.
  • the compressor could be started off-line (not from the beginning of filling).
  • the useful operating time of the compressor initially 1, 12 min could be reduced to 0.72 min for example.
  • the invention makes it possible, for example, to reduce the size and the power of the compressor required.
  • the energetic gains of the invention are more or less important.
  • the invention can be applied to any other type of gas than hydrogen.
  • the invention can be applied to an installation (station) using several storage sources 2 sources connected in parallel and used successively or simultaneously).

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Automation & Control Theory (AREA)
  • Thermal Sciences (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP16707847.6A 2015-02-04 2016-01-28 Procédé et un dispositif de remplissage de réservoir d'hydrogène Withdrawn EP3254015A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR1550847A FR3032257B1 (fr) 2015-02-04 2015-02-04 Procede et un dispositif de remplissage de reservoir d'hydrogene
PCT/FR2016/050178 WO2016124838A1 (fr) 2015-02-04 2016-01-28 Procédé et un dispositif de remplissage de réservoir d'hydrogène

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US11015763B2 (en) * 2016-02-23 2021-05-25 Tokico System Solutions, Ltd. Expansion turbine and compressor-type high-pressure hydrogen filling system and control method for same
FR3086993B1 (fr) * 2018-10-09 2021-11-26 Air Liquide Procede et installation de stockage et de distribution d'hydrogene liquefie
FR3088701B1 (fr) * 2018-11-15 2020-10-23 Air Liquide Installation et procede de remplissage de reservoirs de gaz sous pression
CN109458549A (zh) * 2018-12-27 2019-03-12 浙江海畅气体有限公司 一种高压瓶充装系统温度控制装置
FR3098274B1 (fr) * 2019-07-03 2022-01-28 Air Liquide Dispositif et procédé de remplissage de réservoirs.
CN110375194B (zh) * 2019-07-05 2023-12-22 北京国家新能源汽车技术创新中心有限公司 一种液氢加氢站热管理系统
FR3106393B1 (fr) * 2020-01-20 2021-12-10 Air Liquide Station et un procédé de remplissage de réservoir(s).
CN112283577A (zh) * 2020-11-04 2021-01-29 太原理工大学 一种车载高压氢气分级充注系统
CN114046442B (zh) * 2021-08-02 2023-06-06 有研工程技术研究院有限公司 一种多平台压型储氢装置及其制造方法
DE102021125688A1 (de) * 2021-10-04 2023-04-06 Schmöle GmbH Wärmetauscher und Verfahren zum Betanken eines Fahrzeuges

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JP4050019B2 (ja) * 2001-08-09 2008-02-20 本田技研工業株式会社 ボイルオフガス処理装置
JP5055883B2 (ja) * 2005-09-07 2012-10-24 トヨタ自動車株式会社 水素供給装置
JP4753696B2 (ja) * 2005-11-29 2011-08-24 本田技研工業株式会社 水素充填装置
JP4760353B2 (ja) * 2005-12-14 2011-08-31 トヨタ自動車株式会社 液体水素タンク残量検知システム
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JP4803602B2 (ja) * 2007-02-06 2011-10-26 株式会社日本製鋼所 水素充填装置
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JP3143795U (ja) * 2008-05-26 2008-08-07 ダイソーブレーン株式会社 フルオロカーボンの移充填回収装置
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FR3006742B1 (fr) * 2013-06-05 2016-08-05 Air Liquide Dispositif et procede de remplissage d'un reservoir

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JP6692824B2 (ja) 2020-05-13
FR3032257A1 (fr) 2016-08-05
CN107208840B (zh) 2019-05-31
CN107208840A (zh) 2017-09-26
JP2018505360A (ja) 2018-02-22
WO2016124838A1 (fr) 2016-08-11
US20180023763A1 (en) 2018-01-25
FR3032257B1 (fr) 2017-07-14
US10451219B2 (en) 2019-10-22
CA2975581A1 (en) 2016-08-11

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