EP1717510B1 - Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch - Google Patents

Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch Download PDF

Info

Publication number
EP1717510B1
EP1717510B1 EP06112218A EP06112218A EP1717510B1 EP 1717510 B1 EP1717510 B1 EP 1717510B1 EP 06112218 A EP06112218 A EP 06112218A EP 06112218 A EP06112218 A EP 06112218A EP 1717510 B1 EP1717510 B1 EP 1717510B1
Authority
EP
European Patent Office
Prior art keywords
container
filling
gas
filled
filling gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Not-in-force
Application number
EP06112218A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP1717510A2 (de
EP1717510A3 (de
Inventor
Hermann Grabhorn
Friedhelm Herzog
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.)
Messer Group GmbH
Original Assignee
Messer Group 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
Application filed by Messer Group GmbH filed Critical Messer Group GmbH
Publication of EP1717510A2 publication Critical patent/EP1717510A2/de
Publication of EP1717510A3 publication Critical patent/EP1717510A3/de
Application granted granted Critical
Publication of EP1717510B1 publication Critical patent/EP1717510B1/de
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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
    • F17C5/06—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
    • F17C13/00—Details of vessels or of the filling or discharging of vessels
    • F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/021—Special adaptations of indicating, measuring, or monitoring equipment having the height as the parameter
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F17C7/04—Discharging liquefied gases with change of state, e.g. vaporisation
    • 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
    • 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
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/04—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
    • F17C2223/042—Localisation of the removal point
    • F17C2223/046—Localisation of the removal point in the liquid
    • 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
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/04—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by other properties of handled fluid after transfer
    • F17C2225/042—Localisation of the filling point
    • F17C2225/046—Localisation of the filling point in the liquid
    • 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
    • F17C2227/0337—Heat exchange with the fluid by cooling
    • F17C2227/0341—Heat exchange with the fluid by cooling using another fluid
    • 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
    • F17C2250/0408—Level of content in 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
    • F17C2250/06—Controlling or regulating of parameters as output values
    • F17C2250/0605—Parameters
    • F17C2250/0626—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
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/06—Controlling or regulating of parameters as output values
    • F17C2250/0605—Parameters
    • F17C2250/0631—Temperature
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2260/00—Purposes of gas storage and gas handling
    • F17C2260/02—Improving properties related to fluid or fluid transfer
    • F17C2260/025—Reducing transfer time
    • 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

Definitions

  • the invention relates to a method for filling a container with a filling gas or filling gas mixture.
  • this method is suitable for inexpensively filling pressure vessels permitted for pressures of 700 bar or more.
  • this is suitable Method for filling small-volume tanks, in particular gas generators for airbags, fuel tanks for gas-powered vehicles or fuel cell systems.
  • a refueling device is known by means of which vehicle tanks are filled with liquid cryogenic fuel.
  • a dosing tank is received within a pressure vessel which is filled with a heat exchange means for subcooling the dosing. By subcooling ensures that the fuel remains in the tank to be filled during filling in the liquid state and so relatively short refueling periods can be realized.
  • a filling of a pressure vessel with gas is not provided in this item.
  • Object of the present invention is therefore to provide a way to fill pressure vessels with gases or components of gas mixtures, in which the filled gas is set as accurately as possible.
  • the container to be filled is flow-connected to a metering container.
  • the dosing is maintained by means of a heat exchange medium to a temperature which is below the boiling point of the filling gas or the Basgaskomponente, but above its melting temperature or its pour point.
  • the container to be filled is in a bath containing a heat exchange medium of the same or another type, in heat exchange with the Heat exchange medium and is maintained at a temperature lower than the temperature in the dosing.
  • the filling gas or the filling gas component is therefore present in the dosing container in the liquid but not in the boiling state and can be determined very accurately in its quantity.
  • the heat exchange medium for the metering container and / or for the container to be filled is a liquefied gas whose boiling temperature is varied by adjusting the pressure.
  • the temperature of the gas can be adjusted in a wide range according to the requirements and in particular kept at a value which is sufficiently far above the freezing point or the pour point of the filling gas, so that the filling process is not disturbed by ice deposits.
  • the container to be filled with the same heat exchange medium is heated, which is also provided for controlling the temperature of the dosing, wherein the temperature difference between the containers is realized by different pressures of the heat exchange medium.
  • a further embodiment of the invention provides that the container partially filled with one or more filling gas components is subsequently filled with a filling gas component held in the gaseous state.
  • the mixing ratio of the gaseous Gugaskomponente to the other Gugaskomponenten can be advantageously adjusted by varying the gas pressure of the gaseous component.
  • the filled container is then filled with a gas mixture whose composition is known with great accuracy.
  • a device for filling a container with a filling gas or a filling gas mixture is provided with a metering, the Heat exchanger surfaces is in thermal contact with a heat exchange medium and is equipped with a filling gas supply for supplying the filling gas or a filling gas component in the liquid or gaseous state and with a filling line for connecting the container to be filled.
  • the tempered dosing container allows the supply of a liquefied filling gas or a filling gas component at a temperature below its boiling point and thus without the disturbing influences that would occur during boiling of the filling gas.
  • the device of the dosing is arranged in a provided for receiving the heat exchange means pressure vessel.
  • the dosing container is received in a bath of heat exchange medium, the temperature of which can be adjusted in a targeted manner by varying the pressure in the pressure vessel. The heat transfer between the heat exchange medium and the filling gas via the walls of the dosing.
  • a further advantageous embodiment of the invention provides that the container to be filled is added during its filling in a fillable with a heat exchange medium bath.
  • the metering container is advantageously equipped with a control device for fixing the liquid level in the metering container.
  • a control device for fixing the liquid level in the metering container may be, for example, an overflow, or a measuring and control device which prevents the addition of filling gas above a certain filling level.
  • the device 1 for filling a container 2 with a filling gas or filling gas mixture comprises a metering container 3, which is accommodated in the interior of a pressure vessel 4.
  • a gas supply line 6 for supplying filling gas in the gaseous state in its upper region.
  • the gas supply line 6 is connected to a vent line 7.
  • Gas supply line 6 and vent line 7 can be closed or opened with valves 8.9.
  • a liquid gas feed line 11 opens for supplying a liquefied filling gas.
  • the liquefied gas supply line 11 is provided with a fitting 12, which can be actuated by means of a control device 13 as a function of a measured liquid level 14 in the interior of the metering container 3.
  • the dosing 3 is equipped with a filling line 15, which in the operating state of the device 1 via a releasable connection means 10 establishes the flow connection to the container 2 to be filled.
  • the filling line 15 is equipped with a shut-off valve 16.
  • the pressure vessel 4 provided with an insulation 17, which is only partially shown here, is shut off with a supply line 18 for a heat exchange medium.
  • a valve 19 is arranged, which can be controlled by means of a controller 20 in response to a measured liquid level 21 in the interior of the pressure vessel 4.
  • a Gäsab In an upper region of the pressure vessel 4, a Gäsabtechnisch 22 opens.
  • a device 23 for pressure control ensures the maintenance of a certain pressure in the pressure vessel. 4
  • the container 2 should be filled with the most precisely metered amounts of argon and helium.
  • the dosing tank 3 is first filled via the liquid gas supply line 11 with liquid argon, which was taken from a storage container, not shown here in liquid form.
  • the dosing tank 3 is accommodated in the pressure tank 4 in a bath of a coolant, in the example liquid nitrogen.
  • the liquid nitrogen is supplied to the pressure vessel via the supply line 18. The heat exchange between the dosing tank 3 and the liquid nitrogen bath via the walls of the dosing 3.
  • the nitrogen evaporates in the pressure vessel 4 partially and thus increases the pressure in the pressure vessel 4.
  • the pressure in the pressure vessel to a maintained predetermined value of, for example, about 3 bar.
  • the liquid nitrogen in the pressure vessel 4 is at a temperature of about minus 187 ° C, ie at a temperature below the boiling point of argon under normal pressure conditions (minus 186 ° C) or at higher pressures, but above the melting point of Argon (minus 189 ° C) is.
  • the present in the dosing 3 at a low pressure of, for example, about 1.1 bar argon is thus in the liquid, but not in the boiling state. In this state, the liquid argon is easy to handle and in particular allows the exact filling of the dosing container 4 up to a predetermined liquid level 14th
  • the valve 12 is completely closed and the valve 16 is opened.
  • the argon flows into the container 2.
  • the container 2 is received in an insulated dip tank 25 and is also cooled with liquid nitrogen.
  • the nitrogen in Tauchbad einer 25 has a lower pressure than in the pressure vessel 4, for example, atmospheric pressure, and is therefore at a lower temperature.
  • the argon vapor pressure in the container 1 is always lower than in the dosing tank 2, so that the filling process is not hindered by evaporating argon.
  • the liquid nitrogen in the dip tank 25 at atmospheric pressure its temperature is minus 196 ° C and the filled argon in the container 2 freezes. The resulting suction effect (cryopump effect) supports and accelerates the filling process.
  • the filling of the container 1 with liquid argon is also possible if the connecting device 10 is not gas-tight, but designed in the manner of a syringe: Furthermore, instead of the previously described filling of the dosing 3 with liquid argon and argon in the gaseous state on the Gas supply 6 are introduced, which then liquefied in the dosing 3 by the heat dissipation through the container wall of the dosing 3. Instead of the metering container 3 receiving pressure vessel 4 or in addition to this, the temperature in the metering 4 can also be adjusted by another technique, such as a heat exchanger.
  • the metered addition of a further gas which can be supplied in the liquid or gaseous state takes place.
  • gaseous helium is introduced via the gas supply line 6 into the metering tank 3.
  • the control of the amount of gas supplied takes place by regulating the pressure in the gas supply line 6 or in the metering 3.
  • the helium remains in the metering 3 in the gaseous state.
  • the addition of helium can take place after the cached in the dosing 3 Argon has been completely filled in the container;
  • the supply of helium on the gas supply line 6 already make during the argon filling of the container 2 and thus to accelerate the filling of the container 2 in total as a result of the gas pressure.
  • shut-off valve 16 After completion of the Heliumbe Chelfung the shut-off valve 16 is closed, the container 2 is closed and separated from the connecting device 10. The metering container 3 is depressurized by opening the valve 9, and the device 1 is available for filling a further container available.
  • the container 1 can be decoupled from the device 1 in a different procedure even after filling with argon and transported to a..weiteren filling device in which then the Heliumb, e hypolEung done. Because of the low argon vapor pressure in the container 1 escapes during transport almost no argon from the container 2, even if it is not closed for the transport process. This approach has the advantage that existing helium-Follanlagen could be used for this purpose.
  • the device 1 is also suitable for filling containers with gas mixtures, which consist of more than two components. In this case, the individual components are added successively in the manner described above. The device 1 enables accurate and rapid filling of containers 2 with low filling pressure and an exactly predictable final pressure.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP06112218A 2005-04-25 2006-04-04 Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch Not-in-force EP1717510B1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102005019413A DE102005019413A1 (de) 2005-04-25 2005-04-25 Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch

Publications (3)

Publication Number Publication Date
EP1717510A2 EP1717510A2 (de) 2006-11-02
EP1717510A3 EP1717510A3 (de) 2008-07-09
EP1717510B1 true EP1717510B1 (de) 2011-09-14

Family

ID=36273435

Family Applications (1)

Application Number Title Priority Date Filing Date
EP06112218A Not-in-force EP1717510B1 (de) 2005-04-25 2006-04-04 Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch

Country Status (4)

Country Link
EP (1) EP1717510B1 (zh)
CN (2) CN100552278C (zh)
AT (1) ATE524691T1 (zh)
DE (1) DE102005019413A1 (zh)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101315545B (zh) * 2008-06-27 2010-06-09 浙江大学 一种加氢站高效加氢的三级氢气加注系统
JP5332933B2 (ja) * 2009-06-17 2013-11-06 トヨタ自動車株式会社 水素充填システム
CN102494514B (zh) * 2011-12-09 2014-10-15 张立永 冻堆
KR102282129B1 (ko) * 2013-05-17 2021-07-26 엔테그리스, 아이엔씨. 고압 bf3/h2 혼합물의 제조
CN104075104B (zh) * 2014-06-24 2016-02-10 北京控制工程研究所 卫星电推进系统热增压氙气加注方法
DE102014112059A1 (de) * 2014-08-22 2016-02-25 Proton Motor Fuel Cell Gmbh Brennstoffzellensystem-Reaktionsgasbehälter mit optimierter Raumausnutzung
CN109312896A (zh) * 2016-04-15 2019-02-05 斯科特科技公司 针对特定呼吸气瓶的各种气体和污染物的实时分析记录
ITUA20163553A1 (it) * 2016-05-18 2017-11-18 Vrv S P A Contenitore di stoccaggio, trasporto e distribuzione di gas liquidi o liquefatti
CN107747678A (zh) * 2017-11-13 2018-03-02 国网内蒙古东部电力有限公司检修分公司 一种极寒地区高压电气设备混合气体补气装置
CN109444218B (zh) * 2018-12-17 2024-02-20 西南科技大学 一种氧化动力学反应中改进的环境状态模拟装置及使用方法
CN111425755A (zh) * 2019-12-13 2020-07-17 凯馺国际股份有限公司 一种气泡水机用钢瓶中气体的填充设备及其填充方法

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL6512548A (zh) * 1965-09-28 1967-03-29
DE1501291A1 (de) * 1966-12-24 1969-12-04 Max Planck Gesellschaft Vorrichtung zur Nachfuellung eines Heliumbades bei Temperaturen bis unterhalb des ?-Punktes und Betriebsverfahren hierzu
DE3003355A1 (de) * 1980-01-31 1981-08-06 Messer Griesheim Gmbh, 6000 Frankfurt Verfahren zum transport und zur speicherung permanenter gase
DE3714424C1 (de) * 1987-04-30 1988-06-09 Messerschmitt Boelkow Blohm Speicherung von Edelgas fuer elektrische Raumfahrtantriebe
JPH10259898A (ja) * 1997-01-14 1998-09-29 Daikin Ind Ltd 液化ガスの移充填方法
DE19704362C1 (de) * 1997-02-05 1998-01-02 Linde Ag Betankungseinrichtung für kryogene Kraftstoffe und Verfahren zum Betanken von Fahrzeugen jeder Art mit unterkühlter Flüssigkeit aus einer derartigen Betankungseinrichtung
US5860282A (en) * 1997-07-24 1999-01-19 Winterlab Limited Process for preparing ice substitutes
US5960633A (en) * 1998-05-14 1999-10-05 Limbach; John N. Apparatus and method for transporting high value liquified low boiling gases
DE10107895B4 (de) * 2001-02-20 2007-07-05 Air Liquide Deutschland Gmbh Verfahren und Vorrichtung zum Befüllen von Druckbehältern mit tiefsiedenden permanenten Gasen oder Gasgemischen
EP1353112A1 (en) * 2002-04-10 2003-10-15 Linde Aktiengesellschaft Cryogenic liquid transfer method
FR2840971B1 (fr) * 2002-06-12 2004-08-06 Air Liquide Procede de stockage en phase gazeuse d'un fluide compressible et dispositif de stockage correspondant
US6688115B1 (en) * 2003-01-28 2004-02-10 Air Products And Chemicals, Inc. High-pressure delivery system for ultra high purity liquid carbon dioxide

Also Published As

Publication number Publication date
CN101180495A (zh) 2008-05-14
CN1854596B (zh) 2010-06-09
EP1717510A2 (de) 2006-11-02
CN1854596A (zh) 2006-11-01
ATE524691T1 (de) 2011-09-15
EP1717510A3 (de) 2008-07-09
CN100552278C (zh) 2009-10-21
DE102005019413A1 (de) 2006-10-26

Similar Documents

Publication Publication Date Title
EP1717510B1 (de) Verfahren und Vorrichtung zum Befüllen eines Behälters mit einem Füllgas oder Füllgasgemisch
DE69934923T2 (de) Verfahren zum Befüllen von Flaschen mit kryogenem Fluid
EP1364152B1 (de) Verfahren und vorrichtung zum befüllen von druckbehältern mit tiefsiedenden permanenten gasen oder gasgemischen
EP2035739B1 (de) Verfahren zum betrieb einer vorrichtung zur befüllung eines behälters mit kryogen gespeichertem kraftstoff
EP2863103B1 (de) Vorrichtung und Verfahren zum Unterkühlen von Kohlendioxid
EP1695001A1 (de) Verfahren zur gasbefüllung von druckgasbehältern
EP1381807B1 (de) Druckbehälter
EP1180637A2 (de) Vorrichtung und Verfahren zur druckgeregelten Versorgung aus einem Flüssiggastank mit einem Wärmetauscher
DE102006025657B4 (de) Vorrichtung zur Förderung von kryogen gespeichertem Kraftstoff
DE102017008210A1 (de) Vorrichtung und Verfahren zum Befüllen eines mobilen Kältemitteltanks mit einem kryogenen Kältemittel
EP1846691B1 (de) Verfahren und vorrichtung zum befüllen von druckbehältern mit nicht verflüssigten gasen oder gasgemischen
DE3114319C1 (de) Verfahren zum Betanken eines mit einem Wasserstoffhydridspeicher ausgerüsteten Fahrzeugs
EP0849550B1 (de) Verfahren zur Kühlung eines Verbrauchers auf Tieftemperatur und Flüssiggas-Kühlungssystem zur Durchführung des Verfahrens
EP1379807B1 (de) Verfahren und vorrichtung zum lagern von flüssigkeiten und verflüssigten gasen
EP2711601A2 (de) Verfahren zum Befüllen eines Kältemitteltanks eines Kühlfahrzeugs sowie Kühlfahrzeug
DE102008001710A1 (de) Verfahren und Vorrichtung zur Reduzierung der Korrosionsneigung in einem Flüssigkeitskreislauf
DE102010010108B4 (de) Verfahren zur Speicherung von und Speicher für Erdgas
DE4427710B4 (de) Anordnung zur Gasführung und Drucksteuerung an Kaltvergaseranlagen
DE102006025658B4 (de) Verfahren zum Betrieb einer Vorrichtung zur kryogenen Speicherung von Kraftstoff
DE19717621A1 (de) Unterkühlen von flüssigen Gasen
DE102015221537A1 (de) Kraftfahrzeug mit einem Drucktank
DE3128243A1 (de) "druckregelung in einer anlage zur lagerung und abgabe von tiefkalten fluessigen medien"
DE102022000752A1 (de) Vorrichtung und Verfahren zum Befüllen eines Behälters mit komprimierten gasförmigem Wasserstoff
EP3450819A1 (de) Verfahren zum befüllen eines mobilen kältemitteltanks mit einem kryogenen kältemittel
EP3879164A1 (de) Befüllvorrichtung und verfahren zum befüllen

Legal Events

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

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A2

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

AX Request for extension of the european patent

Extension state: AL BA HR MK YU

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

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

AX Request for extension of the european patent

Extension state: AL BA HR MK YU

RIC1 Information provided on ipc code assigned before grant

Ipc: F17C 5/06 20060101ALI20080530BHEP

Ipc: F17C 13/02 20060101ALI20080530BHEP

Ipc: F17C 7/04 20060101ALI20080530BHEP

Ipc: F17C 5/00 20060101AFI20060512BHEP

17P Request for examination filed

Effective date: 20090109

17Q First examination report despatched

Effective date: 20090211

AKX Designation fees paid

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

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

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

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502006010159

Country of ref document: DE

Effective date: 20111110

REG Reference to a national code

Ref country code: NL

Ref legal event code: VDEP

Effective date: 20110914

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: LT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: SE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

LTIE Lt: invalidation of european patent or patent extension

Effective date: 20110914

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20111215

Ref country code: CY

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: SI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: LV

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

RAP2 Party data changed (patent owner data changed or rights of a patent transferred)

Owner name: MESSER GROUP GMBH

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IS

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120114

Ref country code: SK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: IE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: CZ

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: NL

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: RO

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: EE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

Ref country code: PT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20120116

Ref country code: IT

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

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

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DK

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

26N No opposition filed

Effective date: 20120615

REG Reference to a national code

Ref country code: DE

Ref legal event code: R097

Ref document number: 502006010159

Country of ref document: DE

Effective date: 20120615

BERE Be: lapsed

Owner name: MESSER GROUP G.M.B.H.

Effective date: 20120430

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120430

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20120404

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120404

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120430

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120430

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120430

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20111225

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 524691

Country of ref document: AT

Kind code of ref document: T

Effective date: 20120404

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20111214

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120404

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20110914

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20120404

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20060404

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20150430

Year of fee payment: 10

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20150408

Year of fee payment: 10

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502006010159

Country of ref document: DE

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20161230

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20160502

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20161101