EP2565514A1 - Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage - Google Patents

Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage Download PDF

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Publication number
EP2565514A1
EP2565514A1 EP11179317A EP11179317A EP2565514A1 EP 2565514 A1 EP2565514 A1 EP 2565514A1 EP 11179317 A EP11179317 A EP 11179317A EP 11179317 A EP11179317 A EP 11179317A EP 2565514 A1 EP2565514 A1 EP 2565514A1
Authority
EP
European Patent Office
Prior art keywords
storage tank
liquefied gas
subcooler
tanker
cooling bath
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP11179317A
Other languages
German (de)
English (en)
Inventor
Helmut Henrich
Franz Lürken
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.)
Air Liquide Deutschland GmbH
Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Original Assignee
Air Liquide Deutschland GmbH
Air Liquide SA
LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Air Liquide Deutschland GmbH, Air Liquide SA, LAir Liquide SA pour lEtude et lExploitation des Procedes Georges Claude filed Critical Air Liquide Deutschland GmbH
Priority to EP11179317A priority Critical patent/EP2565514A1/fr
Priority to AU2012301199A priority patent/AU2012301199A1/en
Priority to JP2014527581A priority patent/JP2014527606A/ja
Priority to PCT/EP2012/066027 priority patent/WO2013030006A1/fr
Priority to US14/342,138 priority patent/US20140216601A1/en
Priority to EP12753445.1A priority patent/EP2751468A1/fr
Publication of EP2565514A1 publication Critical patent/EP2565514A1/fr
Withdrawn legal-status Critical Current

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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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • F17C2205/0326—Valves electrically actuated
    • 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
    • F17C2221/013—Carbone dioxide
    • 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
    • F17C2221/014—Nitrogen
    • 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
    • F17C2223/0169—Liquefied gas, e.g. LPG, GPL subcooled
    • 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
    • F17C2225/0146—Two-phase
    • F17C2225/0153—Liquefied gas, e.g. LPG, GPL
    • F17C2225/0169—Liquefied gas, e.g. LPG, GPL subcooled
    • 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
    • F17C2225/033—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
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • 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
    • F17C2227/0339—Heat exchange with the fluid by cooling using the same 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
    • F17C2227/0388—Localisation of heat exchange separate
    • 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/06—Fluid distribution
    • F17C2265/063—Fluid distribution for supply of refueling stations
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2270/00—Applications
    • F17C2270/01—Applications for fluid transport or storage
    • F17C2270/0165—Applications for fluid transport or storage on the road
    • F17C2270/0168—Applications for fluid transport or storage on the road by vehicles
    • F17C2270/0171—Trucks

Definitions

  • the present invention relates to a method and apparatus for refilling a storage tank with a supercooled cryogenic liquefied gas from a tanker vehicle.
  • the refrigerated liquefied gas is in particular liquefied nitrogen (LIN).
  • liquefied gas Consumers of refrigerated liquefied gas are usually placed in large-volume storage tanks, from which the consumer can remove the cold-liquefied gas. These storage tanks must be refilled regularly. The refilling takes place by means of tank vehicles, in which the cryogenic liquefied gas is usually transported in a supercooled state in a storage tank. By a supercooled state, it is meant that the cold-liquefied gas has a temperature below the boiling point at a corresponding pressure.
  • the storage tank Before refilling the storage tank is usually under pressure due to the evaporating refrigerant-liquefied gas. This pressure is lowered by venting before the refilling process, whereby further refrigerant-liquefied gas evaporates.
  • the cold liquefied gas stored in the tanker is transferred by the internal pressure in the tanker into the storage tank, with no pumps being used, as this would cause a further temperature increase of the refrigerant liquefied gas. This filling process therefore takes a long time.
  • the cryogenic liquefied gas is preferably cryogenic liquefied argon, cryofied helium, cryogenic liquefied carbon dioxide or most preferably cryogenic liquefied nitrogen (LIN).
  • a storage tank in the sense of the present invention is understood to mean a large-volume tank which is suitable for holding a refrigerated liquefied gas and which is set up in particular in the vicinity of a consumer and can be refilled via a mobile tank vehicle.
  • a tanker vehicle in this sense is a vehicle which is suitable for transporting a refrigerated liquefied gas in a suitable container, in particular a storage tank.
  • a subcooler in the context of the present invention is understood to mean a device for cooling, which has a container receiving a cooling bath, in which a refrigerated liquefied gas can be filled and stored.
  • the cooling bath is located in the subcooler and insulated from the environment.
  • a heat exchanger is also formed, which is in heat exchange with the cooling bath and through which a medium to be cooled can be passed.
  • the feed pump is between the storage tank of the tanker and the Subcooler arranged so that refrigerated liquefied gas can be conveyed from the tanker.
  • the cooling bath of the subcooler is initially preferably filled from the tanker with the liquefied gas.
  • so much liquefied gas is introduced into the cooling bath until a fill level above the heat exchanger arranged in the cooling bath is reached.
  • the tanker is preferably connected to an input of the storage tank, whereby the liquefied gas can be guided through a line system in the storage tank and / or in the cooling bath. Valves are arranged in the line system, by the actuation of which the liquefied gas can be guided either into the cooling bath and / or to the storage tank.
  • the liquefied gas in the cooling bath assumes a substantially constant thermodynamic state.
  • the resulting temperature of the liquefied gas is referred to as the bath temperature and is substantially equal to or only slightly lower than the temperature of the undercooled refrigerated liquefied gas in the tanker vehicle. In particular, a temperature between -195 ° C and -199 ° C can be reached here.
  • liquefied gas from the tanker is directed through the heat exchanger in the subcooler to the storage tank.
  • a supply pump in particular a not separately cooled and / or the tanker associated feed pump, promoted.
  • the energy introduced by the feed pump is partly transferred as heat to the liquefied gas, but the heat is essentially in the heat exchanger of the subcooler transfer the liquefied gas present in the cooling bath, whereby the pumped cold liquefied gas from the tanker is not significantly increased upon reaching the storage tank compared to its starting temperature in the tanker.
  • the conveyed cryogenic liquefied gas is in a liquid state most of the time during production and can be pumped against the pressure prevailing in the storage tank.
  • the subsidized cryogenic liquefied gas is usually also colder than the refrigerated liquefied gas held in the storage tank and further cools it.
  • the advantage of this method is that the cryogenic liquefied gas can be pumped by means of a pump, whereby the time required for the refilling can be reduced by up to 70% compared to a pump without pump. Furthermore, the pump used does not have to be in a low-temperature state at all times, since the heat generated by the pump is absorbed by the cooling bath of the subcooler. Compared to a pump without pump, the process is energetically hardly worse, since only the energy for cooling or cold holding the subcooler must be additionally expended. The subcooler is usually cooled only for the period of refilling and in the meantime assumes the ambient temperature.
  • the filling level and / or the pressure in the cooling bath of the subcooler are kept constant during the refilling of the storage tank.
  • cryogenic liquefied gas is diverted into the cooling bath.
  • valves in the line system which are connected to a control unit, switched accordingly.
  • the control unit also monitors the refill with level sensors and temperature sensors.
  • a vent valve is arranged on the cooling bath, via which the pressure in the cooling bath can be lowered. In this way, constant conditions throughout the refilling process are adjustable.
  • the pressure and / or the temperature in the tanker vehicle are kept constant during the filling of the storage tank. Also by this measure, the conditions are kept constant during the refilling process.
  • the liquefied gas is stored in the storage tank at a pressure between 3 and 15 bar, preferably between 5 and 10 bar and a temperature lower than the boiling temperature of the liquefied gas corresponding to the pressure.
  • a pressure between 3 and 15 bar, preferably between 5 and 10 bar and a temperature lower than the boiling temperature of the liquefied gas corresponding to the pressure.
  • the liquefied gas in the storage tank is in a supercooled state, it being generally possible to assume that the refrigerated liquefied gas in the tanker vehicle is at an even lower temperature.
  • this also means that the pressure in the storage tank relative to the ambient pressure is increased or remains during the refilling process. As a result, can be dispensed with an initial venting of the storage tank, which further time during the refilling process is saved and possibly connected to the storage tank consumers are not exposed to pressure fluctuations.
  • the subcooler is no longer supplied with liquefied gas and therefore warms up. This means that the subcooler is kept at a low bath temperature only during the refilling process by the liquefied gas. Between two refills, the liquefied gas in the subcooler evaporates and the subcooler assumes ambient temperature. Thus, the subcooler does not need to be constantly cooled and can not freeze. Cooling to the refilling process is achieved by filling with the liquefied gas in a short time.
  • an apparatus for refilling a storage tank with a supercooled refrigerated liquefied gas from a tanker vehicle, especially with liquid nitrogen wherein the storage tank is associated with a subcooler with a cooling bath through which the liquefied gas from the tanker is directed into the storage tank can be, wherein the tanker or inlet side of the subcooler, a feed pump is provided with which the liquefied gas can be pumped under pressure through the cooling bath in the storage tank.
  • the device is in particular designed and set up to carry out the method according to the invention.
  • the subcooler is mounted on the tanker or in the vicinity of the storage tank.
  • refilling a storage tank can be done in a short time.
  • means for filling the subcooler with subcooled cryogenic liquefied gas from the tanker vehicle and / or for keeping constant a predeterminable fill level of the cooling bath are provided.
  • These means preferably comprise a line system, valves, sensors and / or a control unit.
  • a line system is provided with valves, which are arranged so that on the one hand, the cooling bath with liquefied gas and / or the storage tank can be filled with liquid gas, wherein the valves are preferably connected to the control unit.
  • the control unit is also connected to level sensors and / or temperature sensors for monitoring the cooling bath and / or the storage tank or the tank vehicle.
  • the storage tank for a storage pressure of 3 to 15 bar, preferably from 5 to 10 bar, designed and the feed pump for a corresponding Print designed.
  • the refilling with a corresponding pressurized liquefied gas is made possible, whereby the refilling time is greatly reduced.
  • a refueling vehicle with a subcooler and a feed pump wherein the subcooler is arranged on the outlet side to the feed pump.
  • a corresponding tanker vehicle is suitable for carrying out the method according to the invention and has, in particular, a suitable storage tank for storing undercooled liquefied gas.
  • the figure shows schematically a device 8 for refilling a storage tank 1 with a supercooled refrigerated liquefied gas.
  • the device 8 comprises a tanker 2 with a storage tank 16 in which the cold-liquefied supercooled gas is delivered.
  • the device 8 further comprises a subcooler 3 with a cooling bath 4, in which a heat exchanger 7 is formed.
  • the subcooler 3 is connected via a line 9 and a feed pump 6 to the storage tank 16 of the tanker vehicle 2, and is further connected via a line 9 to the storage tank 1.
  • the lines 9 and the subcooler 3 form a line system 17, 9 passed over the lines with the aid of the lines of liquefied gas from the storage tank 16 of the tanker vehicle 2 via the heat exchanger 7 either in the cooling bath 4 or in the storage tank 1 can be.
  • two supply valves 10 and a filling valve 13 are provided in the lines 9 and the line system 17.
  • a level sensor 14 and temperature sensors 15 are provided in the subcooler 3.
  • the level sensor 14, the temperature sensors 15 and the supply valves 10 and the filling valve 13 are connected via signal lines 11 to a control unit 18, which monitors the refilling process.
  • the subcooler 3 also has a vent valve 12. Also on the line 9, a vent valve 12 is provided.
  • the storage tank 16 of the tanker 2 is connected via the pump 6 to the subcooler 3.
  • the cooling bath 4 of the subcooler 3 is filled with cold-liquefied gas from the storage tank 16 to a filling level 5, which is above the heat exchanger 7.
  • the supply valve 10 is opened in the line 9 to the subcooler and the supply valve to the storage tank 1 is closed, wherein the filling valve 13 is opened.
  • the cryogenic liquefied gas is supplied from the storage tank 16 of the tanker 2 via the pipe 9 and the supply pump 16 through the heat exchanger 7 to the storage tank 1.
  • the supply valves 10 are opened and the filling valve 13 is closed.
  • the storage tank 1 can also be filled by means of a supply pump 6, whereby the time for the refilling can be kept very short.
  • the teaching of the invention enables a fast refilling of a storage tank 1 by a tanker 2, whereby a single tanker 2 can fill up a higher number of storage tanks per day. Tank vehicles 1 and their staff can thus be used much more effectively.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP11179317A 2011-08-30 2011-08-30 Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage Withdrawn EP2565514A1 (fr)

Priority Applications (6)

Application Number Priority Date Filing Date Title
EP11179317A EP2565514A1 (fr) 2011-08-30 2011-08-30 Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage
AU2012301199A AU2012301199A1 (en) 2011-08-30 2012-08-16 Method and device for refilling a storage tank
JP2014527581A JP2014527606A (ja) 2011-08-30 2012-08-16 貯蔵タンクに補充する方法および装置
PCT/EP2012/066027 WO2013030006A1 (fr) 2011-08-30 2012-08-16 Procédé et dispositif pour remplir une cuve de stockage
US14/342,138 US20140216601A1 (en) 2011-08-30 2012-08-16 Method and Device for Refilling a Storage Tank
EP12753445.1A EP2751468A1 (fr) 2011-08-30 2012-08-16 Procédé et dispositif pour remplir une cuve de stockage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
EP11179317A EP2565514A1 (fr) 2011-08-30 2011-08-30 Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage

Publications (1)

Publication Number Publication Date
EP2565514A1 true EP2565514A1 (fr) 2013-03-06

Family

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Family Applications (2)

Application Number Title Priority Date Filing Date
EP11179317A Withdrawn EP2565514A1 (fr) 2011-08-30 2011-08-30 Procédé et dispositif destinés au remplissage supplémentaire d'un réservoir de stockage
EP12753445.1A Withdrawn EP2751468A1 (fr) 2011-08-30 2012-08-16 Procédé et dispositif pour remplir une cuve de stockage

Family Applications After (1)

Application Number Title Priority Date Filing Date
EP12753445.1A Withdrawn EP2751468A1 (fr) 2011-08-30 2012-08-16 Procédé et dispositif pour remplir une cuve de stockage

Country Status (5)

Country Link
US (1) US20140216601A1 (fr)
EP (2) EP2565514A1 (fr)
JP (1) JP2014527606A (fr)
AU (1) AU2012301199A1 (fr)
WO (1) WO2013030006A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014170583A1 (fr) * 2013-04-18 2014-10-23 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procédé et installation d'alimentation d'au moins un poste d'usinage en liquide cryogénique sous-refroidi
CN104930342A (zh) * 2015-06-12 2015-09-23 上海正帆科技有限公司 一种高纯砷烷的钢瓶充装装置和方法
EP3196534A1 (fr) * 2016-01-22 2017-07-26 Air Liquide Deutschland GmbH Procédé, système de ravitaillement en carburant et unité de condensation et de sous-refroidissement pour le remplissage de réservoirs avec un combustible tel que du gaz naturel liquide
CN109084172A (zh) * 2018-08-29 2018-12-25 江苏省特种设备安全监督检验研究院 液化气罐车余气残液回收装置

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US9821425B2 (en) 2014-03-05 2017-11-21 5Me Ip, Llc Device for supplying subcooled liquid cryogen to cutting tools
US11924930B2 (en) 2015-08-31 2024-03-05 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US20170119046A1 (en) 2015-10-30 2017-05-04 British American Tobacco (Investments) Limited Apparatus for Heating Smokable Material

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Publication number Priority date Publication date Assignee Title
WO2014170583A1 (fr) * 2013-04-18 2014-10-23 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procédé et installation d'alimentation d'au moins un poste d'usinage en liquide cryogénique sous-refroidi
FR3004784A1 (fr) * 2013-04-18 2014-10-24 Air Liquide Procede et installation d'alimentation d'au moins un poste d'usinage en liquide cryogenique sous-refroidi
CN104930342A (zh) * 2015-06-12 2015-09-23 上海正帆科技有限公司 一种高纯砷烷的钢瓶充装装置和方法
EP3196534A1 (fr) * 2016-01-22 2017-07-26 Air Liquide Deutschland GmbH Procédé, système de ravitaillement en carburant et unité de condensation et de sous-refroidissement pour le remplissage de réservoirs avec un combustible tel que du gaz naturel liquide
CN109084172A (zh) * 2018-08-29 2018-12-25 江苏省特种设备安全监督检验研究院 液化气罐车余气残液回收装置

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US20140216601A1 (en) 2014-08-07
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JP2014527606A (ja) 2014-10-16
WO2013030006A1 (fr) 2013-03-07

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