WO2006114137A1 - Two-step-process for filling gas containers for airbag systems and gas filling device for a two-step-filling process - Google Patents

Two-step-process for filling gas containers for airbag systems and gas filling device for a two-step-filling process Download PDF

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Publication number
WO2006114137A1
WO2006114137A1 PCT/EP2006/000713 EP2006000713W WO2006114137A1 WO 2006114137 A1 WO2006114137 A1 WO 2006114137A1 EP 2006000713 W EP2006000713 W EP 2006000713W WO 2006114137 A1 WO2006114137 A1 WO 2006114137A1
Authority
WO
WIPO (PCT)
Prior art keywords
gas
container
gas container
filling
process according
Prior art date
Application number
PCT/EP2006/000713
Other languages
French (fr)
Inventor
Friedel Michel
Lutz Thiedecke
Ulrich Klebe
Hans Hiller
Thorsten Frank
Friedel Theissen
Original Assignee
L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude
Air Liquide Deutschland Gmbh
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from DE102005019413A external-priority patent/DE102005019413A1/en
Priority claimed from FR0552500A external-priority patent/FR2889730B1/en
Application filed by L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude, Air Liquide Deutschland Gmbh filed Critical L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude
Priority to EP06706445A priority Critical patent/EP1877695A1/en
Priority to US11/912,519 priority patent/US20080202629A1/en
Publication of WO2006114137A1 publication Critical patent/WO2006114137A1/en

Links

Classifications

    • 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
    • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/02—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with liquefied gases
    • F17C5/04—Methods 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
    • 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
    • F17C5/00—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures
    • F17C5/06—Methods or apparatus for filling containers with liquefied, solidified, or compressed gases under pressures for filling with compressed 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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • 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
    • F17C2201/0138—Shape tubular
    • 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
    • F17C2201/058—Size portable (<30 l)
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602—Wall structures; Special features thereof
    • F17C2203/0612—Wall structures
    • F17C2203/0614—Single wall
    • F17C2203/0617—Single wall with one layer
    • 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
    • F17C2205/0311—Closure means
    • 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
    • F17C2209/00—Vessel construction, in particular methods of manufacturing
    • F17C2209/22—Assembling processes
    • F17C2209/221—Welding
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/016—Noble gases (Ar, Kr, Xe)
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/01—Pure fluids
    • F17C2221/016—Noble gases (Ar, Kr, Xe)
    • F17C2221/017—Helium
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0107—Single phase
    • F17C2223/0123—Single phase gaseous, e.g. CNG, GNC
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0107—Single phase
    • F17C2223/013—Single phase liquid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0107—Single phase
    • F17C2223/0138—Single phase solid
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • 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
    • F17C2225/0107—Single phase
    • F17C2225/0123—Single phase gaseous, e.g. CNG, GNC
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • 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
    • F17C2225/036—Very high pressure, i.e. above 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
    • 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
    • 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03—Heat exchange with the fluid
    • F17C2227/0367—Localisation of heat exchange
    • F17C2227/0369—Localisation of heat exchange in or on a vessel
    • F17C2227/0376—Localisation of heat exchange in or on a vessel in wall contact
    • F17C2227/0383—Localisation of heat exchange in or on a vessel in wall contact outside the vessel
    • 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
    • F17C2250/043—Pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/02—Mixing fluids
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/02—Mixing fluids
    • F17C2265/025—Mixing fluids different fluids
    • 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
    • F17C2270/0181—Airbags
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2270/00—Applications
    • F17C2270/05—Applications for industrial use
    • F17C2270/059—Mass bottling, e.g. merry belts

Definitions

  • the invention concerns a process for filling a high pressure gas container and a device for filling a high pressure gas container, in particular a gas container for airbag systems.
  • a fuel gas is filled into a light weight tank made with a liner of chrome nickel steel inside of a fibre reinforced shell, wherein the fuel is introduced in deep cooled liquid form and is stored at a pressure above 300 bar.
  • a pressure vessel for example of an airbag system, is filled with a gas or a gas mixture at a temperature which is higher than the boiling point thereof, closing the cold vessel and a pressure is produced in the filled and closed vessel by heating it to ambient temperatures.
  • a pressure container is filled with a gas mixture, wherein a gas mixture is introduced in its gaseous state or in its liquefied state or at least one gas component of a gas mixture is introduced in its gaseous state or in its liquefied state in a cooled pressure gas container.
  • US 1,414,359 discloses a process for filling compressed gas containers, wherein a given quantity of liquefied gas is placed in a vessel of low specific heat capacity that is suspended within the container, the container is closed, and the walls of the container are maintained at a temperature above 0 0 C until the enclosed substance has been converted into gaseous form.
  • DE 101 19 115 discloses a pressure container particularly suited for filling with low boiling permanent gases or gas mixtures at low temperatures which is provided on its inner surface with a material having a low heat conducting coefficient.
  • EP 0 033 386 discloses a process for transporting and storing permanent gases, in particular hydrogen, under pressure in pressure containers, wherein the gases are cooled to low temperatures above their boiling point and are transported and stored in isolated pressure containers.
  • Chemical generators which generate gas by reaction of a chemical solid with ambient air
  • Hybrid generators which use both a fuel solid and gas that is stored in a pressurized high pressure gas container; - Cold gas generators that store gas in pressurized gas containers at high pressures up to 700 bar at 15°C.
  • the gas generators which are filled with various gases at ambient temperatures, provide for considerable technical problems, both in terms of their production and their filling with pressures of up to 700 bar or above.
  • the heat of compression in particular during a rapid filling leads to undefined temperature conditions which usually considerably affect the metering precision with which the amount of gas is introduced into the gas containers.
  • To meet a high metering standard is important with respect to the subsequent inflation characteristics of the airbag.
  • Very expensive and complex piston or diaphragm compressors are required to generate the very high pressures. This entails high investment and high maintenance costs.
  • a correspondingly complex and expensive downstream gas supply is required for these pressures.
  • An object of the present invention is to provide for a process respectively a device for filling a high pressure gas container with pressures up to 1000 bar or above which is efficient, reliable and reproducible yet economical and quick and allows for a precise metering of the amount of gas that is introduced into the container.
  • a process for filling a high pressure gas container comprises the following steps:
  • the first gas may be liquefied cryogenically or may be solidified cryogenically meaning that the phase transition from the gaseous state to the liquefied respectively solidified state is performed through cooling of the first gas.
  • the determination and the control of the amount of gas that is filled into the gas container may be performed manometrically, volumetrically gravimetrically, and/or by opening time of a valve.
  • the high pressure gas container is in particular for airbag systems.
  • the first gas and/or the second gas may be an inert gas, in particular a noble gas.
  • Gases used in connection with airbag systems may be argon, oxygen, nitrogen, hydrogen, helium, dinitrogen monoxide (N 2 O) as pure gases or mixtures thereof.
  • the first gas may be argon
  • the second gas may be helium.
  • the high pressure gas container may also be used in connection with fuel cells for storing fuel gases such as hydrogen.
  • the boiling temperature of the first gas is in particular lower than the boiling temperature of the second gas.
  • the ratio of the gas particles density of the first gas to the gas particles density of the second gas in the filled gas container may range from 1:1 to 100:1, in particular from 5:1 to 10:1.
  • the first gas may be a pure gas or a mixture of gases.
  • the second gas may be a pure gas or a mixture of gases.
  • the first gas is supplied into the gas container at low temperatures, in particular below 200 0 K 5 in particular below 10O 0 K.
  • As the first gas is liquefied or solidified only small amounts of compression heat is generated during the introducing step of the first gas into the gas container such that the degree of efficiency of the fill- ing process is increased. As much less compression heat is generated, the temperature conditions of the filling process are much better defined. Consequently, the amount of the gases supplied respectively introduced into the gas container may be metered much more precisely.
  • the liquefied first gas may be introduced into the gas container by completely immersing the gas container into a bath of liquefied first gas such that the first gas enters the gas container.
  • the gas container prior to immersing the gas container, the gas container may be precooled in a separate cooling bath, such as a cooling bath of liquid nitrogen.
  • the cooling of the gas container Due to ,the cooling of the gas container the temperature of the gas container as well as the temperature of the gas content inside of the gas container is well- defined. A tight control of the temperature allows for precise controlling the amount of gas supplied into the gas container.
  • the cooling of the gas container may be stopped or at least interrupted.
  • the gas container may be transported from a supplying unit for supplying the first gas to an introducing unit for introducing the second gas.
  • the heat capacity of the gas container as well as of the first gas supplied into the gas containers helps to stabilize the temperature of and in the gas container and the second gas may be introduced at comparatively low pressures, in particular below 200 bars, advantageously below 100 bars, eventhough it may be introduced at a ambient tempera- tares. A precise metering of the amount of gases filled into the gas container is facilitated.
  • conventional introducing units that are designed for comparatively low pressures in particular below 200 bar, advantageously below 100 bars, without them being adapted to operate at extremely low temperatures such as below 100 0 K.
  • the second gas may be precooled before being introduced into the gas container.
  • the temperature of the second gas may be about the temperature of the first gas, in particular may be below 200 0 K, in particular below 100 0 K.
  • the gas container is closed.
  • the closing may be performed using a membrane valve and/or may be performed by welding.
  • the pressure within the gas container at 15°C may be in the range from 250 bar to 1300 bar, in particular in the range from 500 bar to 800 bar.
  • the cooling of the gas container may be performed in a cooling bath, in particular a cooling bath of liquid nitrogen, and a cooling may be stopped by disconnecting the gas container from the cooling bath.
  • the gas container may be completely immersed in a cooling bath containing the first gas.
  • the gas container may also be precooled prior to the supplying step of the first gas. With help of the cooling bath the temperature of the gas container is tightly controlled.
  • the process allows for tight metering control also in cases of batching the filling processes for a multitude of gas containers. This is important as the final pressure strongly influences the operating characteristics of the filled gas container in its use.
  • the cooling bath may be kept under a pressure other than ambient pressure, in particular above ambient pressure, such as in the range from 1.4 bar to 50 bar, in particular from 2 bar to 10 bar, in order to provide for a desired temperature in the cooling bath.
  • a third gas which is liquefied may be used as cooling medium in the cooling bath.
  • the gas container may be temporarily closed.
  • a temporal closing of the gas container may facilitate the transport of the gas container from the supplying unit, which supplies the first gas into the gas container, to the introducing unit, which introduces the second gas into the gas container.
  • the temporal closing of the gas container helps to avoid or at least reduce evaporation losses and helps to increase the metering precision.
  • the gas container may be temporarily closed using an auxiliary valve.
  • the auxiliary valve may be a ball cock, a ball valve, a bibcock, a butterfly valve, a gate valve, a globe valve, check valve, a rotary valve, a piston valve or any other valve that is able to temporarily close the gas container suitably.
  • the final respectively permanent closing of the gas container may be performed by welding.
  • the first gas and/or the second gas may be a mixture of pure gases.
  • the gas con- tainers may be adapted and destined for use in airbag systems.
  • the gas container may also be adapted and destined for use in fuel cells.
  • the supplying of the first gas may be performed at a pressure in the range from 0,2 bar to 15 bar, in particular in the range from 0,5 bar to 4 bar.
  • the supplying of the second gas is performed at a pressure in the range from 2 bar to 100 bar , in particular in the range from 5 bar to 50 bar , for example in the range from 10 bar to 20 bar .
  • the pressure values are meant to be absolute and not with respect to ambient pressure.
  • the first gas may be supplied in a liquid state into the gas container and solidifies in the gas container.
  • the gas container respectively the first gas needs to be colder than the freezing temperature of the second gas.
  • the first gas may be supplied at a temperature lower than its boiling temperature, in particular at least I 0 K, preferably at least 2°K, lower than its boiling tempera- ture, and at a temperature higher than its freezing temperature, in particular at least 1°K, preferably at least 2°K, higher than its freezing temperature.
  • the gas container may be connected to a sealing device, in particular a welding apparatus, and after the introducing step of the second gas the gas container is sealed by the sealing device, in particular by welding.
  • the described two-step process provides for more freedom with respect to organizing the individual process steps.
  • comparatively simple devices in particular conventional sealing devices or introducing units for introducing the second gas, that are not adapted to high pressure or low temperature appliances, may be used.
  • complexity of the filling process as well as investments and development cost are considerably reduced.
  • Due to the two-step structure the- cold filling technique may still be combined with the conventional sealing technology known from high temperature filling without the need of complex adaptation of the conventional devices to the cold temperature environment.
  • the advantages of the cold filling process with respect to its metering precision and its high thermodynamic efficiency may still be enjoyed as eventhough the sealing device may operate at ambient temperature, the gas containers may remain at low temperatures.
  • the pressures involved in the gas con- tainer during the filling process may thus be kept well below 250 bar, in particular well below 100 bar.
  • the cooling of the gas container may be performed using a liquefied third gas in particular liquid nitrogen, wherein in particular the temperature of the third gas is controlled by controlling the pressure in the third gas.
  • the gas container may be cooled before the supplying step of the first gas.
  • the gas container may be precooled in the cooling bath prior to the supplying step of the first gas.
  • the device for filling high pressure gas containers comprises:
  • a stopping unit for stopping the cooling of the gas container '
  • An introducing unit for introducing a gaseous second gas into the gas container after the supplying step of the first gas
  • a unit for closing the gas container A unit for closing the gas container.
  • the device is in particular adapted for carrying out the process according to the invention.
  • the device is in particular destined for carrying out the process accord- ing to the invention.
  • the introducing unit may be at a separate location of the supplying unit and may be displaced therefrom.
  • the stopping unit transports the gas container from the supplying unit to the introducing unit.
  • the stopping unit may disconnect the gas container from a cooling unit for cooling the gas container.
  • the cooling unit may be a cooling bath in which the gas container is at least partially immersed.
  • the unit for closing the gas container may comprise a welding apparatus.
  • the device may further comprise a transport mechanism for transporting the gas containers through the cooling bath.
  • the transport mechanism at least partially immerses the gas container before the gas containers are connected to the supplying unit, transports the gas container to the supplying unit where the gas container are filled with the first gas and transports the gas containers from the supplying unit to the introducing unit, where the gas container are connected with the introducing unit and are filled with the second gas.
  • the transport mechanism transports the gas containers from the introducing unit to the unit for closing the gas container.
  • the unit for closing the gas container may be a welding apparatus.
  • the stopping unit may be provided as being part of the transport mechanism.
  • the device may be for filling high pressure gas containers for airbag systems or for fuel cells.
  • the device may further comprise a gas supply station and at least one thermally isolated filling tube with a tube head that is in fluid connection with the gas supply station, wherein the filling tube is for supplying the first gas to the gas con- tainers.
  • the tube head is moveable and may be positioned by a positioning device.
  • the filling tube is flexible and helps to establish the connection between the gas container and the gas supply station. The flexible filling tube is particularly advantageous when a multiplicity of gas containers need to be filled and a fast connecting of the gas container with the gas supply station, is desired.
  • Fig. 1 shows the two-step process according to the invention
  • Fig. 2 shows a high pressure gas container to be used according to the invention shown in cross section;
  • Fig. 3 shows further high pressure gas container to be used according to the invention shown in cross section
  • Fig. 4 shows a detailed view of a supplying unit of a filling device according to the invention.
  • Fig. 5 shows a supplying unit of a further embodiment of the filling device according to the invention.
  • Fig. 1 shows schematically the two-step process for filling a high pressure gas container 1 with argon as a first gas 2 and helium as a second gas 3 using a supplying unit 7 for supplying the first gas 2 into the gas container 1 and an introducing unit 9 for introducing the second gas 3 into the gas container 1.
  • the gas container 1 comprises a container body 26 for receiving the first gas 2 and the second gas 3 and is connected to an auxiliary valve 5.
  • the gas container 1 is connected to a cooling bath 4 which comprises a third gas 6 which is liquefied in order to pre- cool the gas container 1 down to 86°K which is a temperature a little bit below the boiling temperature of argon.
  • the third gas 6 is liquid nitrogen (boiling temperature of which is 77°K at normal pressure) which is kept under a slight pressure in the cooling bath 4 in order to provide for 86°K in the cooling bath 4.
  • This precool- ing is performed using a precooling unit 24 which at least partially immerses the gas container 1 in the cooling bath 4.
  • the gas container 1 is then transported with a transport mechanism 12 to a supplying unit 7 for supplying liquid argon as first gas 2 into the gas container 1.
  • the auxiliary valve 5 is closed in order to diminish evaporation losses of the first gas 2.
  • the cooling of the gas container 1 is stopped by disconnecting the gas container 1 from the cooling bath 2 by a stopping unit 8 and is transported to an introducing unit for introducing the second gas 3 in its gaseous state.
  • the second gas 3 such as helium is taken from a second container 22 and is evaporated by an evaporator 25 and is introduced through the auxiliary valve 5.
  • the unit 10 for closing comprises a sealing device 11 which seals the gas container 1 by welding.
  • Both the introducing unit 9 and the unit 10 for closing may be of a conventional type meaning that they do not need to be adapted for cryogenical temperatures and do not need to be capable of coping with high pressures above 300 bar.
  • the second gas 3 is introduced at ambient temperature into the gas container 1. After closing the gas container 1 the gas container 1 are allowed to warm up to ambient temperatures such that the pressure inside of the container body 26 rises to a well-defined pressure around 600 bar.
  • the first gas 2 may be supplied at a pressure ranging from 0,5 bar to 3 bar and the second gas 3 maybe introduced at 15 bar.
  • the amount of gas supplied respectively introduced into the gas container 1 may be controlled volumetrically, gravimetrically or by an opening time of a metering valve.
  • the second gas may be metered according to the partial pressure that is eventually desired at room temperature. This metering may be performed outside of the cooling bath 4 for instance in the sealing device 11.
  • Fig. 2 shows a gas container 1 in cross section to be used according to the invention.
  • the gas container 1 comprises the auxiliary valve 5 in a first connection line 28 to the container body 26 and a first valve 27 in a second connection line 29 to the container body 26.
  • the first valve 27 is provided at the container body 26 be- fore the beginning of the filling process.
  • the first valve 27 is a membrane valve and is adapted to be opened at the instance of operation of the gas container 1 for example during the operation of the airbag system (not shown).
  • the first valve 27 operates non-reversibly, i.e. opens only once.
  • the first valve 27 may be welded to the container body 26 respectively to the second connection line 29.
  • the auxiliary valve 5 is for facilitating the supplying of the first gas 2 respectively the introducing of the second gas 3 into the container body 26.
  • the auxiliary valve 5 is for temporarily closing the container body 26 such that evaporation losses are reduced.
  • the auxiliary valve 5 is closed.
  • the auxiliary valve 5 may also be closed in between the supplying and the introducing step.
  • Fig. 3 shows a further gas container 1 in cross section to be used according to the invention, wherein the first valve 27 and the auxiliary valve 5 are in a fluid series connection 30.
  • the permanent closing of the container body 26 is real- ized by the first valve 27 which is closed after the filling of the container body 26 with a gas 2, 3 or a mixture of gases 2, 3.
  • the auxiliary valve 5 is used for facilitating the supplying of the first gas and/or the introducing of the second gas 3.
  • Fig. 4 shows schematically the supplying unit 7 comprising a gas supply station 13 with a flexible filling tube 14 which is to be connected to the container 1.
  • a tube head 15 is provided which comprises a metering valve 17.
  • the tube head 15 is positioned at the gas container 1 with a positioning device 16. Due to the flexibility of the filling tube 14 a gas tight connection between the gas supply station 13, respectively the sup- plying unit 7, and the gas container 1 is established in a short time.
  • the filling tube 14 is thermally isolated and comprises a gas channel 18 for supplying the first gas 2 into the gas container 1.
  • the gas channel 18 is isolated by means of an insulation vacuum.
  • the filling tube 14 is doubled walled.
  • a heat shield 19 is introduced, which is at least partially actively cooled.
  • the moveable tube head 15 allows for a fast connection which is important if a multiplicity of gas containers 1 need to be filled.
  • Fig. 5 shows a further embodiment of a supplying unit 7 of the device for filling gas containers 1.
  • Liquid argon is stored as first gas 2 in a large supply tank 33 and is supplied through a supply tube 32 into a first container 21 which also serves as phase separator 20.
  • the liquid argon from the phase separator 20 is precooled in a second precooling unit 35 for precooling the second gas 2.
  • the liquid argon is cooled to 2°K below its boiling point in order to avoid any formation of gas bub- bles within the liquid phase, which might affect the metering precision of the amount of gas supplied into the gas container 1.
  • the second precooling unit 35 uses liquid nitrogen as third gas 6 from a third container 23 which is connected to the second precooling unit 35 with conduits 34.
  • the precooled liquid argon is then supplied with the filling tube 14 to the gas container 1.
  • the filling tube 14 comprises a moveable tube head 15 which may be positioned precisely at the gas container 1.
  • the gas container 1 is transported through the cooling bath by a transport mechanism 12.
  • the cooling bath 4 is closed with a cover 36 in order to establish a pressure in the cooling bath 4 with which the temperature in the cooling bath is precisely controlled.
  • An advantageous process for filling high pressure gas containers 1 comprises the steps: Supplying a liquefied or solidified first gas 2 from a gas supply station 13 through a thermally insulated filling tube 14 with a movable tube head 15 to the high pressure gas container 1.
  • the gas container 1 may be cooled, in particular by a cooling bath 4.
  • the filling tube 14 is in particular cooled at least partially along its length, in particular by the cooling bath 4.
  • the filling tube 14 may be filled using a two step filling process, in which after the supplying step of the first gas 2, a gaseous second gas 3, in particular Helium, is introduced into the gas container 1, wherein in particular during the supplying step of the first gas 2, the gas container 1 is cooled, in particular by a cooling bath 4, and before or during the introducing step of the second gas 3 the cooling of the gas container 1 is stopped, in particular the gas container 1 is taken out of the cooling bath 4.
  • Advantageously high pressure gas containers 1 for air bag systems or for fuel cells are filled.
  • the first gas 2 and / or the second gas 3 may be a mixture of gases.
  • An advantageous process of batch filling of high pressure gas containers 1 with gas comprises the step cooling multiple gas containers 1 in parallel, which are filled sequentially using the process according to the invention.
  • An advantageous arrangement for filling high pressure gas containers 1 with gas comprises a gas supply station 13 and multiple high pressure gas containers 1, wherein the gas supply station 13 comprises at least one thermally insulated filling tube 14 with a movable tube head 15 for gas filling of the gas containers 1, wherein the arrangement may comprise a positioning device 16 for moving the tube head 15 to the individual gas containers 1.
  • a metering valve 17 for controlling a gas flow through the filling tube 14 may be provided in the tube head 15.
  • the gas supply station 13 may comprise a cooling bath 4 for cooling the gas containers I 3 wherein the filling tube 14 may be at least partially immersed in the cooling bath 4 and wherein the arrangement may further comprise a transport mechanism 12 for transporting the gas containers 1 through the cooling bath 4.
  • the filling tube 14 may be at least doubled walled and may comprise an insulation vacuum for thermal insulation.
  • the filling tube 14 may be actively cooled by a cooling medium, in particular a liquefied third gas 6 and / or may comprise a gas channel 18 and a tubular heat shield 19 at least partially around the gas channel 18, wherein the heat shield 19 is cooled by the cool- ing medium.
  • Tube head 15 may comprise an auxiliary valve 5 for temporarily closing the gas container 1.
  • the gas filling tube 14 is in particular for filling a liq- uefied first gas 2 into the gas containers 1.
  • the gas supply station 13 may comprise a first container 21 for a liquefied first gas 2.
  • the gas supply station 13 may advantageously comprise an introducing unit 9 for introducing a gaseous second gas 3 into the gas container 1.
  • the gas supply station 13 may comprise a second container 22 for a liquefied second gas 3, wherein the gas supply station 13 may comprise an evaporator 25 for converting the liquefied second gas 3 into its gaseous state.
  • the gas supply station 13 may comprise a third container 23 for a liquefied third gas 6 as cooling medium.
  • An advantageous gas supply station 13 for filling high pressure gas containers 1 with gas is adapted and in particular destined for use in the arrangement according to the invention.
  • An advantageous high pressure gas container 1 with a container body 26 for stor- ing gas and at least one first valve 27 for discharging the stored gas is characterized by further comprising an auxiliary valve 5 for introducing the gas into the container body 26 and for temporarily closing the container body 26 until the container body 26 is sealed permanently, wherein the first valve 27 and the auxiliary valve 5 are in fluid connection with the container body 26, wherein in particular the first valve 27 and the auxiliary valve 5 may be connected to the container body 26 with separate fluid connection lines 28, 29, or, wherein in particular the first valve 27 and the auxiliary valve 5 may be connected to the container body 26 in a fluid series connection 30.
  • the first valve 27 may be non-reversibly openable.
  • the auxiliary valve 5 may be reversibly openable and closable.
  • a sealing portion 31 may be provided at the auxiliary valve 5 for permanently closing the auxiliary valve 5, wherein in particular the sealing portion 31 may be provided in the fluid connection between the auxiliary valve 5 and the container body 26, or, wherein in particular the auxiliary valve 5 may be provided in the fluid interconnection between the sealing portion 31 and the container body 26.
  • the auxiliary valve 5 may be one of the following valves: a ball cock, a ball valve, a bibcock, a butterfly valve, a gate valve, a globe valve, a check valve, a rotary valve, or a piston valve.
  • the first valve 27 may in particular be a membrane valve.
  • the high pressure gas container 1 may be adapted and/or destined for an air bag system, or, the high pressure gas container 1 may be adapted and/or destined for a fuel cell.
  • An advantageous process for filling a high pressure gas container 1 having a container body 26 for storing gas, at least one first valve 27 for discharging the stored gas and an auxiliary valve 5, wherein the first valve 27 and the auxiliary valve 5 are in fluid connection with the container body 26, comprises the following steps: The gas is introduced into the container body 26 through the auxiliary valve 5; the auxiliary valve 5 is at least temporarily closed; the auxiliary valve 5 is sealed permanently, wherein in particular the auxiliary valve 5 may be sealed by welding. The auxiliary valve 5 may also or instead be sealed by the first valve 27. Prior to filling the container body 26 with gas, the first valve 27 may be provided and may be configured at the gas container 1.
  • the invention concerns a process respectively a device for filling a high pressure gas container 1, comprising the following steps: Supplying a liquefied or solidified first gas 2 into a gas container 1 while the gas container 1 is being cooled; stopping the cooling of the gas container 1 after the supplying step of the first gas; then introducing a gaseous second gas 3 into the gas container 1 and closing the gas container 1.
  • the invention allows for a efficient, reproducible, reliable and economical filling of high pressure gas containers 1, in particular for airbag systems or for fuel cells, and allows to use conventional devices for introducing gases respectively closing gas containers that are not particularly adapted for low temperature respectively high pressure applications.

Abstract

The invention concerns a process respectively a device for filling a high pressure gas container (1), comprising the following steps: Supplying a liquefied or solidified first gas (2) into a gas container (1) while the gas container (1) is being cooled; stopping the cooling of the gas container (1) after the supplying step of the first gas; then introducing a gaseous second gas (3) into the gas container (1) and closing the gas container (1). The invention allows for a efficient, reproducible, reliable and economical filling of high pressure gas containers (1), in particular for airbag systems or for fuel cells, and allows to use conventional devices for introducing gases respectively closing gas containers that are not particularly adapted for low temperature respectively high pressure applications.

Description

EP2006/000713
Two-Step-Process for Filling Gas Containers for Airbag Systems and Gas Filling Device for a Two-Step-Filling Process
The invention concerns a process for filling a high pressure gas container and a device for filling a high pressure gas container, in particular a gas container for airbag systems.
For cold filling pressure containers, according to DE 101 07 895 a gas is cooled before its introduction into a pressure container, wherein on completion of the filling process the pressure container is sealed in a pressure-tight manner. As the gas warms up the pressure in the pressure container rises rapidly.
According to DE 198 17 324 a fuel gas is filled into a light weight tank made with a liner of chrome nickel steel inside of a fibre reinforced shell, wherein the fuel is introduced in deep cooled liquid form and is stored at a pressure above 300 bar.
According to WO 2005/043033 a pressure vessel, for example of an airbag system, is filled with a gas or a gas mixture at a temperature which is higher than the boiling point thereof, closing the cold vessel and a pressure is produced in the filled and closed vessel by heating it to ambient temperatures.
According to WO 2005/059431 a pressure container is filled with a gas mixture, wherein a gas mixture is introduced in its gaseous state or in its liquefied state or at least one gas component of a gas mixture is introduced in its gaseous state or in its liquefied state in a cooled pressure gas container.
US 1,414,359 discloses a process for filling compressed gas containers, wherein a given quantity of liquefied gas is placed in a vessel of low specific heat capacity that is suspended within the container, the container is closed, and the walls of the container are maintained at a temperature above 00C until the enclosed substance has been converted into gaseous form.
DE 101 19 115 discloses a pressure container particularly suited for filling with low boiling permanent gases or gas mixtures at low temperatures which is provided on its inner surface with a material having a low heat conducting coefficient.
EP 0 033 386 discloses a process for transporting and storing permanent gases, in particular hydrogen, under pressure in pressure containers, wherein the gases are cooled to low temperatures above their boiling point and are transported and stored in isolated pressure containers.
It is known, that airbags in vehicles are increasingly using new types of gas gen- erators, which in the event of an accident inflate the airbag within a few milliseconds. High pressure gas storage systems are used as gas generators.
Three different types of gas generators are currently in use:
Chemical generators which generate gas by reaction of a chemical solid with ambient air;
, Hybrid generators which use both a fuel solid and gas that is stored in a pressurized high pressure gas container; - Cold gas generators that store gas in pressurized gas containers at high pressures up to 700 bar at 15°C.
The gas generators, which are filled with various gases at ambient temperatures, provide for considerable technical problems, both in terms of their production and their filling with pressures of up to 700 bar or above. The heat of compression in particular during a rapid filling leads to undefined temperature conditions which usually considerably affect the metering precision with which the amount of gas is introduced into the gas containers. To meet a high metering standard is important with respect to the subsequent inflation characteristics of the airbag. Very expensive and complex piston or diaphragm compressors are required to generate the very high pressures. This entails high investment and high maintenance costs. In addition, a correspondingly complex and expensive downstream gas supply is required for these pressures.
The known cold filling techniques avoid the problem originating from the filling of high pressures, however, these techniques usually work at extremely low temperatures which makes multiple adaptations of conventional process steps, such as the sealing of the gas container, to the low temperature conditions necessary, which is not desirable with respect investment and maintenance costs.
An object of the present invention is to provide for a process respectively a device for filling a high pressure gas container with pressures up to 1000 bar or above which is efficient, reliable and reproducible yet economical and quick and allows for a precise metering of the amount of gas that is introduced into the container.
This and other problems are solved according to the invention by the process respectively device for filling a high pressure gas container as defined in the claims below. Further advantageous embodiments and developments which can be employed individually or in any suitable combination are also provided.
According to the invention a process for filling a high pressure gas container comprises the following steps:
Supplying a liquefied or solidified first gas into a gas container while the gas container is being cooled; - Stopping the cooling in the gas container after the supplying step of the first gas; then Introducing a second gas into the gas container; Closing the gas container.
The first gas may be liquefied cryogenically or may be solidified cryogenically meaning that the phase transition from the gaseous state to the liquefied respectively solidified state is performed through cooling of the first gas.
The determination and the control of the amount of gas that is filled into the gas container may be performed manometrically, volumetrically gravimetrically, and/or by opening time of a valve.
The high pressure gas container is in particular for airbag systems.
The first gas and/or the second gas may be an inert gas, in particular a noble gas. Gases used in connection with airbag systems may be argon, oxygen, nitrogen, hydrogen, helium, dinitrogen monoxide (N2O) as pure gases or mixtures thereof. Advantageously, the first gas may be argon, the second gas may be helium.
The high pressure gas container may also be used in connection with fuel cells for storing fuel gases such as hydrogen.
The boiling temperature of the first gas is in particular lower than the boiling temperature of the second gas.
The ratio of the gas particles density of the first gas to the gas particles density of the second gas in the filled gas container may range from 1:1 to 100:1, in particular from 5:1 to 10:1.
The first gas may be a pure gas or a mixture of gases. The second gas may be a pure gas or a mixture of gases. The first gas is supplied into the gas container at low temperatures, in particular below 2000K5 in particular below 10O0K. As the first gas is liquefied or solidified, only small amounts of compression heat is generated during the introducing step of the first gas into the gas container such that the degree of efficiency of the fill- ing process is increased. As much less compression heat is generated, the temperature conditions of the filling process are much better defined. Consequently, the amount of the gases supplied respectively introduced into the gas container may be metered much more precisely.
The liquefied first gas may be introduced into the gas container by completely immersing the gas container into a bath of liquefied first gas such that the first gas enters the gas container. For this purpose, prior to immersing the gas container, the gas container may be precooled in a separate cooling bath, such as a cooling bath of liquid nitrogen.
Due to ,the cooling of the gas container the temperature of the gas container as well as the temperature of the gas content inside of the gas container is well- defined. A tight control of the temperature allows for precise controlling the amount of gas supplied into the gas container.
After supplying the first gas into the gas container and before introducing the second gas into the gas container, the cooling of the gas container may be stopped or at least interrupted. Between the supplying step and the introducing step the gas container may be transported from a supplying unit for supplying the first gas to an introducing unit for introducing the second gas. The heat capacity of the gas container as well as of the first gas supplied into the gas containers helps to stabilize the temperature of and in the gas container and the second gas may be introduced at comparatively low pressures, in particular below 200 bars, advantageously below 100 bars, eventhough it may be introduced at a ambient tempera- tares. A precise metering of the amount of gases filled into the gas container is facilitated. By this provision it is possible to use conventional introducing units that are designed for comparatively low pressures in particular below 200 bar, advantageously below 100 bars, without them being adapted to operate at extremely low temperatures such as below 1000K.
In a specific embodiment the second gas may be precooled before being introduced into the gas container. The temperature of the second gas may be about the temperature of the first gas, in particular may be below 2000K, in particular below 1000K.
After the introducing step of the second gas into the gas container, the gas container is closed. The closing may be performed using a membrane valve and/or may be performed by welding.
After closing the gas container, it may be warmed up to ambient temperature, such that a high pressure builds up within the gas container. The pressure within the gas container at 15°C may be in the range from 250 bar to 1300 bar, in particular in the range from 500 bar to 800 bar.
The cooling of the gas container may be performed in a cooling bath, in particular a cooling bath of liquid nitrogen, and a cooling may be stopped by disconnecting the gas container from the cooling bath. The gas container may be completely immersed in a cooling bath containing the first gas. The gas container may also be precooled prior to the supplying step of the first gas. With help of the cooling bath the temperature of the gas container is tightly controlled.
The process allows for tight metering control also in cases of batching the filling processes for a multitude of gas containers. This is important as the final pressure strongly influences the operating characteristics of the filled gas container in its use. The cooling bath may be kept under a pressure other than ambient pressure, in particular above ambient pressure, such as in the range from 1.4 bar to 50 bar, in particular from 2 bar to 10 bar, in order to provide for a desired temperature in the cooling bath. For this purpose a third gas which is liquefied may be used as cooling medium in the cooling bath.
After the supplying step of the first gas and before the introducing step of the second gas the gas container may be temporarily closed. A temporal closing of the gas container may facilitate the transport of the gas container from the supplying unit, which supplies the first gas into the gas container, to the introducing unit, which introduces the second gas into the gas container. The temporal closing of the gas container helps to avoid or at least reduce evaporation losses and helps to increase the metering precision.
The gas container may be temporarily closed using an auxiliary valve. The auxiliary valve may be a ball cock, a ball valve, a bibcock, a butterfly valve, a gate valve, a globe valve, check valve, a rotary valve, a piston valve or any other valve that is able to temporarily close the gas container suitably.
The final respectively permanent closing of the gas container may be performed by welding.
The first gas and/or the second gas may be a mixture of pure gases. The gas con- tainers may be adapted and destined for use in airbag systems. The gas container may also be adapted and destined for use in fuel cells.
The supplying of the first gas may be performed at a pressure in the range from 0,2 bar to 15 bar, in particular in the range from 0,5 bar to 4 bar. The supplying of the second gas is performed at a pressure in the range from 2 bar to 100 bar , in particular in the range from 5 bar to 50 bar , for example in the range from 10 bar to 20 bar .
The pressure values are meant to be absolute and not with respect to ambient pressure.
In a special embodiment of the invention the first gas may be supplied in a liquid state into the gas container and solidifies in the gas container. For this purpose the gas container respectively the first gas needs to be colder than the freezing temperature of the second gas.
The first gas may be supplied at a temperature lower than its boiling temperature, in particular at least I0K, preferably at least 2°K, lower than its boiling tempera- ture, and at a temperature higher than its freezing temperature, in particular at least 1°K, preferably at least 2°K, higher than its freezing temperature.
After the supplying step of the first gas and before the introducing step of the second gas, the gas container may be connected to a sealing device, in particular a welding apparatus, and after the introducing step of the second gas the gas container is sealed by the sealing device, in particular by welding.
The described two-step process provides for more freedom with respect to organizing the individual process steps. In particular comparatively simple devices, in particular conventional sealing devices or introducing units for introducing the second gas, that are not adapted to high pressure or low temperature appliances, may be used. In consequence complexity of the filling process as well as investments and development cost are considerably reduced. Due to the two-step structure the- cold filling technique may still be combined with the conventional sealing technology known from high temperature filling without the need of complex adaptation of the conventional devices to the cold temperature environment. On the other hand the advantages of the cold filling process with respect to its metering precision and its high thermodynamic efficiency may still be enjoyed as eventhough the sealing device may operate at ambient temperature, the gas containers may remain at low temperatures. The pressures involved in the gas con- tainer during the filling process may thus be kept well below 250 bar, in particular well below 100 bar.
The cooling of the gas container may be performed using a liquefied third gas in particular liquid nitrogen, wherein in particular the temperature of the third gas is controlled by controlling the pressure in the third gas. The gas container may be cooled before the supplying step of the first gas. In particular the gas container may be precooled in the cooling bath prior to the supplying step of the first gas.
According to the invention, the device for filling high pressure gas containers comprises:
A supplying unit for supplying liquefied or solidified first gas into a gas container while the gas container is being cooled;
A stopping unit for stopping the cooling of the gas container; '
An introducing unit for introducing a gaseous second gas into the gas container after the supplying step of the first gas;
A unit for closing the gas container.
The device is in particular adapted for carrying out the process according to the invention. The device is in particular destined for carrying out the process accord- ing to the invention. The introducing unit may be at a separate location of the supplying unit and may be displaced therefrom. In particular the stopping unit transports the gas container from the supplying unit to the introducing unit. The stopping unit may disconnect the gas container from a cooling unit for cooling the gas container. The cooling unit may be a cooling bath in which the gas container is at least partially immersed. The unit for closing the gas container may comprise a welding apparatus. The device may further comprise a transport mechanism for transporting the gas containers through the cooling bath. Advantageously the transport mechanism at least partially immerses the gas container before the gas containers are connected to the supplying unit, transports the gas container to the supplying unit where the gas container are filled with the first gas and transports the gas containers from the supplying unit to the introducing unit, where the gas container are connected with the introducing unit and are filled with the second gas. Advantageously the transport mechanism transports the gas containers from the introducing unit to the unit for closing the gas container. The unit for closing the gas container may be a welding apparatus. The stopping unit may be provided as being part of the transport mechanism.
The device may be for filling high pressure gas containers for airbag systems or for fuel cells.
The device may further comprise a gas supply station and at least one thermally isolated filling tube with a tube head that is in fluid connection with the gas supply station, wherein the filling tube is for supplying the first gas to the gas con- tainers. The tube head is moveable and may be positioned by a positioning device. The filling tube is flexible and helps to establish the connection between the gas container and the gas supply station. The flexible filling tube is particularly advantageous when a multiplicity of gas containers need to be filled and a fast connecting of the gas container with the gas supply station, is desired.
Further details and favourable aspects, which may be applied alone or may be combined in any suitable manner, will be explained with respect to the following drawings, which shall not restrict the scope of the present invention but shall schematically and exemplarily illustrate the invention.
Fig. 1 shows the two-step process according to the invention; Fig. 2 shows a high pressure gas container to be used according to the invention shown in cross section;
Fig. 3 shows further high pressure gas container to be used according to the invention shown in cross section;
Fig. 4 shows a detailed view of a supplying unit of a filling device according to the invention; and
Fig. 5 shows a supplying unit of a further embodiment of the filling device according to the invention.
Fig. 1 shows schematically the two-step process for filling a high pressure gas container 1 with argon as a first gas 2 and helium as a second gas 3 using a supplying unit 7 for supplying the first gas 2 into the gas container 1 and an introducing unit 9 for introducing the second gas 3 into the gas container 1. The gas container 1 comprises a container body 26 for receiving the first gas 2 and the second gas 3 and is connected to an auxiliary valve 5. The gas container 1 is connected to a cooling bath 4 which comprises a third gas 6 which is liquefied in order to pre- cool the gas container 1 down to 86°K which is a temperature a little bit below the boiling temperature of argon. The third gas 6 is liquid nitrogen (boiling temperature of which is 77°K at normal pressure) which is kept under a slight pressure in the cooling bath 4 in order to provide for 86°K in the cooling bath 4. This precool- ing is performed using a precooling unit 24 which at least partially immerses the gas container 1 in the cooling bath 4. The gas container 1 is then transported with a transport mechanism 12 to a supplying unit 7 for supplying liquid argon as first gas 2 into the gas container 1. Then the auxiliary valve 5 is closed in order to diminish evaporation losses of the first gas 2. Subsequently the cooling of the gas container 1 is stopped by disconnecting the gas container 1 from the cooling bath 2 by a stopping unit 8 and is transported to an introducing unit for introducing the second gas 3 in its gaseous state. The second gas 3 such as helium is taken from a second container 22 and is evaporated by an evaporator 25 and is introduced through the auxiliary valve 5. After completion of the introducing the auxiliary valve 5 is temporarily closed until the gas container 1 is permanently closed using a unit 10 for closing the gas container 1. The unit 10 for closing comprises a sealing device 11 which seals the gas container 1 by welding. Both the introducing unit 9 and the unit 10 for closing may be of a conventional type meaning that they do not need to be adapted for cryogenical temperatures and do not need to be capable of coping with high pressures above 300 bar. The second gas 3 is introduced at ambient temperature into the gas container 1. After closing the gas container 1 the gas container 1 are allowed to warm up to ambient temperatures such that the pressure inside of the container body 26 rises to a well-defined pressure around 600 bar. The first gas 2 may be supplied at a pressure ranging from 0,5 bar to 3 bar and the second gas 3 maybe introduced at 15 bar. The amount of gas supplied respectively introduced into the gas container 1 may be controlled volumetrically, gravimetrically or by an opening time of a metering valve. The second gas may be metered according to the partial pressure that is eventually desired at room temperature. This metering may be performed outside of the cooling bath 4 for instance in the sealing device 11.
Fig. 2 shows a gas container 1 in cross section to be used according to the invention. The gas container 1 comprises the auxiliary valve 5 in a first connection line 28 to the container body 26 and a first valve 27 in a second connection line 29 to the container body 26. The first valve 27 is provided at the container body 26 be- fore the beginning of the filling process. The first valve 27 is a membrane valve and is adapted to be opened at the instance of operation of the gas container 1 for example during the operation of the airbag system (not shown). The first valve 27 operates non-reversibly, i.e. opens only once. The first valve 27 may be welded to the container body 26 respectively to the second connection line 29. The auxiliary valve 5 is for facilitating the supplying of the first gas 2 respectively the introducing of the second gas 3 into the container body 26. The auxiliary valve 5 is for temporarily closing the container body 26 such that evaporation losses are reduced. After the supplying step of the first gas 2 respectively after the introducing step of the second gas 3, the auxiliary valve 5 is closed. The auxiliary valve 5 may also be closed in between the supplying and the introducing step. Once the con- tainer body 26 is completely filled with a gas 2, 3 or with a mixture of gases 2, 3 the first connection line 28 is closed using a sealing portion 31 by welding. The closing portion 31 makes sure that after the closing of the gas container 1, gas may not escape from the container body 26 through the first connection line 28. The sealing portion 31 allows for using inexpensive auxiliary valves 5 without limiting the advantages of temporarily closing the container body 26.
Fig. 3 shows a further gas container 1 in cross section to be used according to the invention, wherein the first valve 27 and the auxiliary valve 5 are in a fluid series connection 30. In this case the permanent closing of the container body 26 is real- ized by the first valve 27 which is closed after the filling of the container body 26 with a gas 2, 3 or a mixture of gases 2, 3. The auxiliary valve 5 is used for facilitating the supplying of the first gas and/or the introducing of the second gas 3.
Fig. 4 shows schematically the supplying unit 7 comprising a gas supply station 13 with a flexible filling tube 14 which is to be connected to the container 1. For connecting the filling tube 14 with the gas container 1, a tube head 15 is provided which comprises a metering valve 17. The tube head 15 is positioned at the gas container 1 with a positioning device 16. Due to the flexibility of the filling tube 14 a gas tight connection between the gas supply station 13, respectively the sup- plying unit 7, and the gas container 1 is established in a short time. The filling tube 14 is thermally isolated and comprises a gas channel 18 for supplying the first gas 2 into the gas container 1. The gas channel 18 is isolated by means of an insulation vacuum. For this purpose the filling tube 14 is doubled walled. For further reducing a heat transfer through radiation within the insulation vacuum a heat shield 19 is introduced, which is at least partially actively cooled. The moveable tube head 15 allows for a fast connection which is important if a multiplicity of gas containers 1 need to be filled.
Fig. 5 shows a further embodiment of a supplying unit 7 of the device for filling gas containers 1. Liquid argon is stored as first gas 2 in a large supply tank 33 and is supplied through a supply tube 32 into a first container 21 which also serves as phase separator 20. The liquid argon from the phase separator 20 is precooled in a second precooling unit 35 for precooling the second gas 2. The liquid argon is cooled to 2°K below its boiling point in order to avoid any formation of gas bub- bles within the liquid phase, which might affect the metering precision of the amount of gas supplied into the gas container 1. The second precooling unit 35 uses liquid nitrogen as third gas 6 from a third container 23 which is connected to the second precooling unit 35 with conduits 34. The precooled liquid argon is then supplied with the filling tube 14 to the gas container 1. For this purpose the filling tube 14, comprises a moveable tube head 15 which may be positioned precisely at the gas container 1. The gas container 1 is transported through the cooling bath by a transport mechanism 12. The cooling bath 4 is closed with a cover 36 in order to establish a pressure in the cooling bath 4 with which the temperature in the cooling bath is precisely controlled.
In the following, further aspects, which are related to the present invention, are described. These individual aspects may be employed individually and separately or in any suitable combination with each other respectively one another:
An advantageous process for filling high pressure gas containers 1 comprises the steps: Supplying a liquefied or solidified first gas 2 from a gas supply station 13 through a thermally insulated filling tube 14 with a movable tube head 15 to the high pressure gas container 1. During the supplying step of the first gas 2, the gas container 1 may be cooled, in particular by a cooling bath 4. The filling tube 14 is in particular cooled at least partially along its length, in particular by the cooling bath 4. The filling tube 14 may be filled using a two step filling process, in which after the supplying step of the first gas 2, a gaseous second gas 3, in particular Helium, is introduced into the gas container 1, wherein in particular during the supplying step of the first gas 2, the gas container 1 is cooled, in particular by a cooling bath 4, and before or during the introducing step of the second gas 3 the cooling of the gas container 1 is stopped, in particular the gas container 1 is taken out of the cooling bath 4. Advantageously high pressure gas containers 1 for air bag systems or for fuel cells are filled. The first gas 2 and / or the second gas 3 may be a mixture of gases.
An advantageous process of batch filling of high pressure gas containers 1 with gas, comprises the step cooling multiple gas containers 1 in parallel, which are filled sequentially using the process according to the invention.
An advantageous arrangement for filling high pressure gas containers 1 with gas comprises a gas supply station 13 and multiple high pressure gas containers 1, wherein the gas supply station 13 comprises at least one thermally insulated filling tube 14 with a movable tube head 15 for gas filling of the gas containers 1, wherein the arrangement may comprise a positioning device 16 for moving the tube head 15 to the individual gas containers 1. Advantageously, a metering valve 17 for controlling a gas flow through the filling tube 14 may be provided in the tube head 15. The gas supply station 13 may comprise a cooling bath 4 for cooling the gas containers I3 wherein the filling tube 14 may be at least partially immersed in the cooling bath 4 and wherein the arrangement may further comprise a transport mechanism 12 for transporting the gas containers 1 through the cooling bath 4. In a useful embodiment, the filling tube 14 may be at least doubled walled and may comprise an insulation vacuum for thermal insulation. The filling tube 14 may be actively cooled by a cooling medium, in particular a liquefied third gas 6 and / or may comprise a gas channel 18 and a tubular heat shield 19 at least partially around the gas channel 18, wherein the heat shield 19 is cooled by the cool- ing medium. Tube head 15 may comprise an auxiliary valve 5 for temporarily closing the gas container 1. The gas filling tube 14 is in particular for filling a liq- uefied first gas 2 into the gas containers 1. The gas supply station 13 may comprise a first container 21 for a liquefied first gas 2. The gas supply station 13 may advantageously comprise an introducing unit 9 for introducing a gaseous second gas 3 into the gas container 1. The gas supply station 13 may comprise a second container 22 for a liquefied second gas 3, wherein the gas supply station 13 may comprise an evaporator 25 for converting the liquefied second gas 3 into its gaseous state. The gas supply station 13 may comprise a third container 23 for a liquefied third gas 6 as cooling medium.
An advantageous gas supply station 13 for filling high pressure gas containers 1 with gas is adapted and in particular destined for use in the arrangement according to the invention.
An advantageous high pressure gas container 1 with a container body 26 for stor- ing gas and at least one first valve 27 for discharging the stored gas, is characterized by further comprising an auxiliary valve 5 for introducing the gas into the container body 26 and for temporarily closing the container body 26 until the container body 26 is sealed permanently, wherein the first valve 27 and the auxiliary valve 5 are in fluid connection with the container body 26, wherein in particular the first valve 27 and the auxiliary valve 5 may be connected to the container body 26 with separate fluid connection lines 28, 29, or, wherein in particular the first valve 27 and the auxiliary valve 5 may be connected to the container body 26 in a fluid series connection 30. The first valve 27 may be non-reversibly openable. Alternatively, the auxiliary valve 5 may be reversibly openable and closable. A sealing portion 31 may be provided at the auxiliary valve 5 for permanently closing the auxiliary valve 5, wherein in particular the sealing portion 31 may be provided in the fluid connection between the auxiliary valve 5 and the container body 26, or, wherein in particular the auxiliary valve 5 may be provided in the fluid interconnection between the sealing portion 31 and the container body 26. The auxiliary valve 5 may be one of the following valves: a ball cock, a ball valve, a bibcock, a butterfly valve, a gate valve, a globe valve, a check valve, a rotary valve, or a piston valve. The first valve 27 may in particular be a membrane valve. Advantageously, the high pressure gas container 1 may be adapted and/or destined for an air bag system, or, the high pressure gas container 1 may be adapted and/or destined for a fuel cell.
An advantageous process for filling a high pressure gas container 1 having a container body 26 for storing gas, at least one first valve 27 for discharging the stored gas and an auxiliary valve 5, wherein the first valve 27 and the auxiliary valve 5 are in fluid connection with the container body 26, comprises the following steps: The gas is introduced into the container body 26 through the auxiliary valve 5; the auxiliary valve 5 is at least temporarily closed; the auxiliary valve 5 is sealed permanently, wherein in particular the auxiliary valve 5 may be sealed by welding. The auxiliary valve 5 may also or instead be sealed by the first valve 27. Prior to filling the container body 26 with gas, the first valve 27 may be provided and may be configured at the gas container 1.
The invention concerns a process respectively a device for filling a high pressure gas container 1, comprising the following steps: Supplying a liquefied or solidified first gas 2 into a gas container 1 while the gas container 1 is being cooled; stopping the cooling of the gas container 1 after the supplying step of the first gas; then introducing a gaseous second gas 3 into the gas container 1 and closing the gas container 1. The invention allows for a efficient, reproducible, reliable and economical filling of high pressure gas containers 1, in particular for airbag systems or for fuel cells, and allows to use conventional devices for introducing gases respectively closing gas containers that are not particularly adapted for low temperature respectively high pressure applications. Reference numerals
1 gas container
2 first gas
3 second gas
4 cooling bath
5 auxiliary valve
6 third gas
7 supplying unit
8 stopping unit
9 introducing unit
10 unit for closing
11 sealing device
12 transport mechanism
13 gas supply station
14 filling tube
15 tube head
16 positioning device
17 metering valve
18 gas channel
19 heat shield
20 phase separator
21 first container
22 second container
23 third container
24 precooling unit
25 evaporator
26 container body
27 first valve
28 first connection line second connection line fluid series connection sealing portion supply tube supply tank conduits second precooling unit cover

Claims

Patent claims
1. Process for filling a high pressure gas container (1 ), comprising the following steps: supplying a liquefied or solidified first gas (2) into a gas container (1) while the gas container (1) is being cooled; stopping the cooling of the gas container (1) after the supplying step of the first gas; then introducing a gaseous second gas (3) into the gas container (1); closing the gas container (1).
2. Process according to claim 1, characterized in that the cooling of the gas container (1) is performed in a cooling bath (4), in particular a cooling bath
(4) of liquid nitrogen, and the cooling is stopped by disconnecting the gas container (1) from the cooling bath (4).
3. Process according to claim 1 or 2, characterized in that the first gas (2) and / or the second gas (3) is a mixture of plural gases.
4. Process according to one of the preceding claims, characterized in that the first gas (2) and / or the second gas (3) is an inert gas, in particular a noble gas.
5. Process according to one of the preceding claims, characterized in that after the supplying step of the first gas (2) and before the introducing step of the second gas (3) the gas container (1) is temporarily closed.
6. Process according to claim 5, characterized in that the gas container (1) is temporarily closed using an auxiliary valve (5).
7. Process according to one of the preceding claims, characterized in that the closing of the gas container (1) is performed by welding.
8. Process according to one of the preceding claims, characterized in that the gas containers (1) are for air bag systems.
9. Process according to one of the preceding claims, characterized in that gas containers (1) are for fuel cells.
10. Process according to one of the preceding claims, characterized in that the supplying of the first gas (2) is performed at a pressure in the range from 0,2 bar to 15 bar , in particular in the range from 0,5 bar to 4 bar.
11. Process according to one of the preceding claims, characterized in that the supplying of the second gas (3) is performed at a pressure in the range from 2 bar to 100 bar, in particular, in the range from 5 bar to 50 bar, for example in the range from 10 bar to 20 bar.
12. Process according to one of the preceding claims, characterized in that the first gas (2) is supplied in a liquid state into the gas container (1) and solidifies in the gas container (1).
13. Process according to one of the preceding claims, characterized in that the first gas (2) is supplied at a temperature lower than its boiling temperature, in particular at least 1°K, preferably at least 2° K, lower than its boiling temperature, and at a temperature higher than its freezing temperature, in particular at least I0K5 preferably at least 2° K, higher than its freezing temperature.
14. Process according to one of the preceding claims, characterized in that after the supplying step of the first gas (2) and before the introducing step of the second gas (3), the gas container (1) is connected to a sealing device (11), in particular a welding apparatus (12), and after the introducing step of the second gas (3) the gas container (1) is sealed by the sealing device
(11), in particular by welding.
15. Process according to one of the preceding claims, characterized in that the cooling is performed using a liquefied third gas (6), in particular liquid nitrogen, wherein in particular the temperature of the third gas (6) is controlled by controlling the pressure in the third gas (6).
16. Process according to one of the preceding claims, characterized in that the gas container (1) is cooled before the supplying step of the first gas (2).
17. Device for filling high pressure gas containers (1), comprising a supplying unit (7) for supplying a liquefied or solidified first gas (2) into a gas container (1) while the gas container (1) is being cooled; a stopping unit (8) for stopping the cooling of the gas container (1); an introducing unit (9) for introducing a gaseous second gas (3) into the gas container (1) after the supplying step of the first gas; a unit (10) for closing the gas container (1).
18. Device according to claim 17, further comprising a cooling bath (4) for cooling the gas container (1).
19. Device according to claim 18, further comprising a transport mechanism
(12) for transporting the gas containers (1) through the cooling bath (4).
20. Device according to one of claims 17 to 19, characterized in that the unit (10) for closing the gas container (1) is a welding apparatus (12).
21. Device according to one of claims 17 to 20, characterized in that the de- vice is for filling high pressure gas containers (1) for air bag systems or for fuel cells.
22. Device according to one of claim 17 to 21, further comprising a gas supply station (13) and at least one thermally insulated filling tube (14) with a tube head (15) that is in fluid connection with the gas supply station (13), wherein the filling tube (14) is for supplying the first gas (2) to the gas containers (1).
23. Device according to claim 22, further comprising a positioning device (16) for positioning the tube head (15) at the gas containers (1 ).
PCT/EP2006/000713 2005-04-25 2006-01-27 Two-step-process for filling gas containers for airbag systems and gas filling device for a two-step-filling process WO2006114137A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP06706445A EP1877695A1 (en) 2005-04-25 2006-01-27 Two-step-process for filling gas containers for airbag systems and gas filling device for a two-step-filling process
US11/912,519 US20080202629A1 (en) 2005-04-25 2006-01-27 Two-Step-Process for Filling Gas Containers for Airbag Systems and Gas Filling Device for a Two-Step-Filling Process

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
DE102005019413A DE102005019413A1 (en) 2005-04-25 2005-04-25 Process to charge an automotive airbag cartridge with gas under defined conditions of temperature and pressure
DE102005019413.3 2005-04-25
FR0552500 2005-08-11
FR0552500A FR2889730B1 (en) 2005-08-11 2005-08-11 METHOD FOR FILLING A PRESSURE GAS TANK

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FR2920858A1 (en) * 2007-09-10 2009-03-13 Air Liquide METHOD OF FILLING A GAS CONTAINER UNDER PRESSURE
CN102080764A (en) * 2010-09-17 2011-06-01 富美科技有限公司 Automatic inflating equipment for inflatable bags

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FR2889730B1 (en) * 2005-08-11 2007-09-21 Air Liquide METHOD FOR FILLING A PRESSURE GAS TANK
JP5332933B2 (en) 2009-06-17 2013-11-06 トヨタ自動車株式会社 Hydrogen filling system
KR20130094348A (en) 2010-12-16 2013-08-23 에어 프로덕츠 앤드 케미칼스, 인코오포레이티드 A process for filling a gas storage container
EP2683977A1 (en) * 2011-03-11 2014-01-15 Shell Internationale Research Maatschappij B.V. Hydrogen dispensing process and system
JP5936938B2 (en) * 2012-07-11 2016-06-22 住友重機械工業株式会社 Method for manufacturing a cryogenic regenerator
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