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EP3036471B1 - Liquefied gas filling station combined with a liquefied gas production device - Google Patents

Liquefied gas filling station combined with a liquefied gas production device Download PDF

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Publication number
EP3036471B1
EP3036471B1 EP14790184.7A EP14790184A EP3036471B1 EP 3036471 B1 EP3036471 B1 EP 3036471B1 EP 14790184 A EP14790184 A EP 14790184A EP 3036471 B1 EP3036471 B1 EP 3036471B1
Authority
EP
European Patent Office
Prior art keywords
circuit
fluid
tank
filling station
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.)
Active
Application number
EP14790184.7A
Other languages
German (de)
French (fr)
Other versions
EP3036471A2 (en
Inventor
Guillaume Pages
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.)
Cryostar SAS
Original Assignee
Cryostar SAS
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 Cryostar SAS filed Critical Cryostar SAS
Priority to PL14790184T priority Critical patent/PL3036471T3/en
Publication of EP3036471A2 publication Critical patent/EP3036471A2/en
Application granted granted Critical
Publication of EP3036471B1 publication Critical patent/EP3036471B1/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

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    • 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
    • F17C6/00—Methods and apparatus for filling vessels not under pressure with liquefied or solidified 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
    • 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
    • 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
    • F17C13/00—Details of vessels or of the filling or discharging of vessels
    • F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/025—Special adaptations of indicating, measuring, or monitoring equipment having the pressure 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
    • F17C13/00—Details of vessels or of the filling or discharging of vessels
    • F17C13/02—Special adaptations of indicating, measuring, or monitoring equipment
    • F17C13/026—Special adaptations of indicating, measuring, or monitoring equipment having the temperature 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
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022—Hydrocarbons, e.g. natural gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0047—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle
    • F25J1/005—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using an "external" refrigerant stream in a closed vapor compression cycle by expansion of a gaseous refrigerant stream with extraction of work
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/006—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the refrigerant fluid used
    • F25J1/007—Primary atmospheric gases, mixtures thereof
    • F25J1/0072—Nitrogen
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0203—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle
    • F25J1/0204—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process using a single-component refrigerant [SCR] fluid in a closed vapor compression cycle as a single flow SCR cycle
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0228—Coupling of the liquefaction unit to other units or processes, so-called integrated processes
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0244—Operation; Control and regulation; Instrumentation
    • F25J1/0245—Different modes, i.e. 'runs', of operation; Process control
    • F25J1/0249—Controlling refrigerant inventory, i.e. composition or quantity
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0257—Construction and layout of liquefaction equipments, e.g. valves, machines
    • F25J1/0262—Details of the cold heat exchange system
    • F25J1/0264—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams
    • F25J1/0265—Arrangement of heat exchanger cores in parallel with different functions, e.g. different cooling streams comprising cores associated exclusively with the cooling of a refrigerant stream, e.g. for auto-refrigeration or economizer
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/02—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures requiring the use of refrigeration, e.g. of helium or hydrogen ; Details and kind of the refrigeration system used; Integration with other units or processes; Controlling aspects of the process
    • F25J1/0243—Start-up or control of the process; Details of the apparatus used; Details of the refrigerant compression system used
    • F25J1/0279—Compression of refrigerant or internal recycle fluid, e.g. kind of compressor, accumulator, suction drum etc.
    • F25J1/0285—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings
    • F25J1/0288—Combination of different types of drivers mechanically coupled to the same refrigerant compressor, possibly split on multiple compressor casings using work extraction by mechanical coupling of compression and expansion of the refrigerant, so-called companders
    • 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
    • F17C2221/032—Hydrocarbons
    • F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, 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
    • F17C2223/01—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
    • F17C2223/03—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
    • F17C2223/035—High pressure (>10 bar)
    • 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
    • F17C2225/0161—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
    • 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
    • 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
    • F17C2225/035—High pressure, i.e. between 10 and 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
    • F17C2225/043—Localisation of the filling point in the gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • 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
    • F17C2227/0355—Heat exchange with the fluid by cooling using another fluid in a closed loop
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    • 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
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    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
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    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
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    • F17C2250/0439—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
    • 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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/06—Fluid distribution
    • F17C2265/063—Fluid distribution for supply of refuelling 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
    • F17C2270/0134—Applications for fluid transport or storage placed above the ground
    • F17C2270/0139—Fuel stations

Definitions

  • the present invention relates to a filling station associated with a device for producing liquefied gas.
  • a service station making it possible to deliver liquefied natural gas from a reservoir.
  • the latter is supplied for example by tank trucks which regularly come to fill the tank.
  • the present invention relates more particularly to a filling station intended for example to fill a tank truck which will supply a tank of a service station delivering liquefied natural gas. More particularly, the present invention relates to a filling station associated with means for producing liquefied natural gas from gas in the gaseous state.
  • a filling station tank is supplied with gas by a gas supply source in the gaseous state which has been treated in order to be in particular freed of its impurities.
  • this gas then passes through a heat exchanger to be liquefied. It is then led into the tank of the filling station.
  • This tank is thus, on the one hand, supplied by the source of gas in the gaseous state and an exchanger and, on the other hand, liquid gas is taken to fill tanks (from a tank truck or boat, or any type of liquefied gas tank).
  • thermodynamic circuit also called a liquefier
  • a fluid is compressed and then expanded to produce cold.
  • the temperatures obtained are well below -160 ° C.
  • Stops and restarts are then managed manually by an operator in charge of managing the filling station.
  • the object of the present invention is therefore to provide a filling station associated with a liquefier for which the production and storage of liquefied (natural) gas are carried out automatically.
  • Another object of the present invention is to provide such a station which can operate without having to stop the operation of the liquefier associated with the filling station.
  • the present invention provides a station for filling liquefied gas and producing liquefied gas as defined by claim 1.
  • a station according to the present invention can automatically produce a liquefied gas thanks in particular to the implementation of a liquefier (second circuit with its exchanger) in which the pressure of the refrigerant is modifiable and has an original regulation based, on the one hand , on the level in the tank and on the temperature of the liquefied gas at a point between the exchanger and the tank and, on the other hand, on an action on the pressure of the refrigerant in the liquefier.
  • a liquefied gas production system is associated with different operating regimes (preferably with a regime corresponding to an idle operating mode) with an original regulation system allowing automated operation.
  • means can also be provided for cooling the fluid after its compression and before its expansion.
  • Several compression and cooling cycles can be provided, for example three successive cycles, followed by a relaxation.
  • the arrangement of the second circuit is for example such that it further comprises means for circulating its refrigerant fluid in the exchanger after its expansion of its refrigerant fluid and for returning it to the compression means so as to achieve a closed cycle. If several compression, cooling and expansion cycles are planned, the refrigerant fluid is preferably brought after reheating in the heat exchanger to the first compression stage.
  • the latter comprises for example a fluid storage tank having, on the one hand, a fluid inlet supplied by a controlled valve arranged downstream of the means making it possible to compress the fluid. fluid and, on the other hand, a fluid outlet controlled by a controlled valve making it possible to inject the fluid contained in the fluid storage tank into the second circuit upstream of the means making it possible to compress the fluid.
  • the second circuit can then be a closed circuit.
  • the fluid used in the second circuit is advantageously nitrogen which is perfectly suited as refrigerant for a variable pressure circuit.
  • the first circuit advantageously comprises a pressure regulating valve arranged upstream of the exchanger. This valve makes it possible to adjust the gas pressure in the first circuit in order to avoid overpressures. It also cuts off the gas supply, which may be necessary in certain specific conditions.
  • An advantageous embodiment of the present invention provides that the system is such that the first circuit and the second circuit comprise a single exchanger in which the fluid of the second circuit circulates in a first direction after expansion and in a second direction, in a second direction.
  • the fluid of the second circuit downstream of the means making it possible to compress the fluid and upstream of the expansion means and, on the other hand, the gas of the first circuit, this gas entering the exchanger in the gaseous state and in coming out in a liquid state. This allows the number of components to be limited without compromising the performance of the system as a whole.
  • control and management system to act on the means for varying the pressure in the second circuit as a function of the temperature measured by the temperature measuring device and in depending on the level of liquefied gas in the tank.
  • An alternative embodiment of the system comprises a piloted valve arranged between the temperature measuring device and the reservoir.
  • the gas circulating in the first circuit is natural gas, in the gaseous or liquid state, and the fluid used in the second circuit is nitrogen (N 2 ) which remains in the state. gaseous.
  • the invention can be applied to a liquefied gas other than natural gas and the refrigerant used in the second circuit can be other than nitrogen.
  • the first circuit has a natural gas inlet 6 regulated in pressure by a pressure regulating valve 8 intended to supply a reservoir 10.
  • the natural gas arrives in the gaseous state at the level of the inlet 6 then is liquefied before arriving in the reservoir 10.
  • a pump 12 is for example used to draw liquefied natural gas out of the tank 10 in order to fill a tank of a tank truck or on a boat, a boat tank, ....
  • the gas at inlet 6 is assumed to be treated. If it is not, a treatment unit (not shown) which purifies the gas, for example by absorption or preferably by adsorption, can be provided.
  • the gas entering the first circuit 2 can, by way of illustrative examples, come from a pipe or else from a biogas or digester production unit.
  • the second circuit forms a combined compression and expansion system hereinafter called a liquefier. It comprises in particular a condenser 14 also linked to the first circuit and intended to ensure the liquefaction of natural gas in this circuit.
  • a desuperheater 18 between the first circuit 2 and the second circuit 4. This desuperheater 18 allows a first cooling of the natural gas coming from the inlet 6 before its introduction into the condenser 14 where it will be liquefied and then stored in the tank 10.
  • the second circuit is here a closed circuit.
  • a motor M drives three compressors C1, C2 and C3 each forming a stage of a compression unit.
  • it is proposed to monitor the nitrogen moving in this circuit.
  • the nitrogen arrives in the compressor C1 via a line R1 and leaves it via a line R2. It then arrives at a first cooler 22 in order to control the temperature of the nitrogen before being returned to the compression unit via a pipe R3.
  • the nitrogen is then compressed by the second compressor C2, then brought through R4 to a second cooler 22 and through R5 to reach a third compression stage of the compression unit.
  • a third cooler 22, connected to the third compressor C3 via an R6 pipe, allows the temperature of the nitrogen at the outlet of the compression unit to be controlled.
  • a pipe R7 leads the nitrogen to a counter-current exchanger 24 then is supplied by R8 to a pressure reducing valve 26.
  • the latter is mechanically linked to the engine M and to the compression unit.
  • the nitrogen is then brought (R9) to the condenser 14 where it absorbs calories from the natural gas that it is desired to liquefy in order to obtain liquefied natural gas (LNG).
  • LNG liquefied natural gas
  • the nitrogen is led (R10) to the desuperheater 18 before reaching through R11 the counter-current exchanger 24 which is connected downstream to the first compressor C1 of the compression unit.
  • a nitrogen storage tank 28 which is used to regulate the quantity of nitrogen in the liquefier, and therefore the pressure of this nitrogen in the second circuit.
  • nitrogen is taken from a part of the second circuit 4 where the pressure is high, for example at the outlet of the compression unit, preferably after the last cooler 22.
  • An inlet valve 30 is used to make such a sample.
  • an outlet valve 32 connects an outlet of the balloon 28 to a portion of the second circuit where the pressure is low. , preferably just upstream of the compression unit and its first compressor C1.
  • the first circuit 2 comprises a filling valve 34 which regulates the flow of liquefied natural gas entering the reservoir 10 and which is arranged upstream of the condenser 14 and of course upstream of the reservoir 10.
  • the object of the present invention is to regulate the filling of the reservoir. 10 as a function of the samples taken from this reservoir by the pump 12.
  • the embodiment of figures 1 and 2 provides for continuous monitoring of the liquid level in the tank 10 and for measuring the temperature downstream of the condenser 14.
  • the level control in the tank 10 is performed by LT sensors known to those skilled in the art and conventionally used to achieve a level measurement in a liquefied natural gas reservoir. These LT sensors are connected to an LC microcontroller which processes the information supplied by the LT sensors.
  • the LC microcontroller also provides a command in the direction of the filling valve 34.
  • a first control loop is thus produced in the management of the liquid level in the reservoir 10.
  • the temperature measurement is performed by a TT sensor which is in turn connected to an XC microcontroller.
  • the latter from the information concerning the temperature in the first circuit 2 downstream of the condenser acts on the inlet valve 30 and on the outlet valve 32 to adapt the quantity of nitrogen in the second circuit 4.
  • the microcontroller XC will tend, according to a predetermined control law, to open the inlet valve 30 in order to withdraw nitrogen out of the second circuit 4. Therefore the absorption calories in natural gas, and therefore also the production of liquefied natural gas, is limited. In this way, a second control loop is realized.
  • the two control loops are linked.
  • the temperature measured by the sensor TT is varied. If from a continuous flow of liquefied natural gas from the condenser 14 to the tank, the filling valve 34 opens, the liquefied natural gas produced at the condenser 14 then fills the tank 10 more quickly and the temperature measured by the TT sensor rises. Conversely, if the filling valve 34 closes, the liquefied natural gas tends to accumulate upstream of the reservoir 10 and the temperature measured by the TT sensor will decrease. There is therefore an interaction physical between the two control loops.
  • the filling valve 34 provided in the alternative embodiments of the figures 1 and 2 can be omitted.
  • the regulation presented here in fact also makes it possible to regulate the entire system.
  • the analysis of the level in the tank makes it possible to know the consumption of liquefied natural gas and the measurement of the temperature downstream of the condenser 14.
  • the only regulation on the pressure of the nitrogen in the second circuit makes it possible to control the gas production.
  • the quantity of gas liquefied by the condenser depends on the calories absorbed by the gas entering the first circuit 2 through the inlet 6.
  • the nitrogen pressure in the second circuit 4 By limiting the nitrogen pressure in the second circuit 4, the calories absorbed at the level of the condenser 14 (and possibly at the level of the desuperheater 18) and therefore the production of liquefied gas are limited.
  • control loop at the input of the first circuit 2.
  • This regulation is a usual regulation on a gas inlet in order to regulate the pressure in the circuit and avoid overpressures which could. be damaging.
  • the regulation of this pressure makes it possible to adjust the pressure in the condenser to a set value.
  • This regulation can also be useful, for example, when the level in the reservoir is high and when the production of liquefied natural gas is reduced, to avoid saturating the condenser with gas in the liquid state.
  • the variants of figures 2 and 3 plan to limit the number of heat exchangers and to combine the condenser 14, the desuperheater 18 and the counter-current exchanger 24 by a single exchanger / condenser 114.
  • the single exchanger / condenser 114 has a central lane traversed in one direction and two lateral lanes traversed in the opposite direction.
  • the central path is taken by the nitrogen at the outlet of the pressure reducer 26 and before its entry into the compression unit.
  • a lateral path is taken by the nitrogen which cools after having been compressed in the compression unit and before its expansion while the other lateral path is taken by the gas which enters the exchanger / condenser 114 at the gaseous state and emerges in the liquid state.
  • the exchanger / condenser 114 may for example be a brazed aluminum plate exchanger.
  • the condenser 14 and / or the countercurrent exchanger 24 can also be exchangers of this type.
  • the refrigeration cycle incorporates a cryogenic nitrogen expansion device which can be regulated by varying the nitrogen pressure in the cycle.
  • the corresponding refrigeration devices allow idling operation which here makes it possible to stop the production of liquefied natural gas without having to stop the refrigeration cycle.
  • the components of the device are maintained at temperature and can thus be used to switch to liquefied gas production mode.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
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  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Description

La présente invention concerne une station de remplissage associée à un dispositif de production de gaz liquéfié.The present invention relates to a filling station associated with a device for producing liquefied gas.

Pour alimenter des véhicules fonctionnant au gaz naturel liquéfié, il est connu d'avoir une station-service permettant de délivrer du gaz naturel liquéfié à partir d'un réservoir. Ce dernier est alimenté par exemple par des camions citernes qui viennent régulièrement remplir le réservoir.To supply vehicles running on liquefied natural gas, it is known to have a service station making it possible to deliver liquefied natural gas from a reservoir. The latter is supplied for example by tank trucks which regularly come to fill the tank.

La présente invention concerne plus particulièrement une station de remplissage destinée par exemple à remplir un camion citerne qui alimentera un réservoir d'une station-service délivrant du gaz naturel liquéfié. Plus particulièrement, la présente invention concerne une station de remplissage associée à des moyens de production de gaz naturel liquéfié à partir de gaz à l'état gazeux.The present invention relates more particularly to a filling station intended for example to fill a tank truck which will supply a tank of a service station delivering liquefied natural gas. More particularly, the present invention relates to a filling station associated with means for producing liquefied natural gas from gas in the gaseous state.

De manière connue, un réservoir de station de remplissage est alimenté en gaz par une source d'alimentation en gaz à l'état gazeux qui a été traité pour être notamment débarrassé de ses impuretés. Tel que décrit dans le document FR 2 714 722 A1 , ce gaz passe alors par un échangeur thermique pour être liquéfié. Il est ensuite conduit dans le réservoir de la station de remplissage. Ce réservoir est ainsi, d'un côté, alimenté par la source de gaz à l'état gazeux et un échangeur et, d'un autre côté, du gaz liquide est prélevé pour remplir des citernes (de camion citerne ou de bateau, ou tout type de réservoir de gaz liquéfié).In a known manner, a filling station tank is supplied with gas by a gas supply source in the gaseous state which has been treated in order to be in particular freed of its impurities. As described in the document FR 2 714 722 A1 , this gas then passes through a heat exchanger to be liquefied. It is then led into the tank of the filling station. This tank is thus, on the one hand, supplied by the source of gas in the gaseous state and an exchanger and, on the other hand, liquid gas is taken to fill tanks (from a tank truck or boat, or any type of liquefied gas tank).

Il est par ailleurs également connu d'utiliser un échangeur, ou condenseur, faisant partie d'un circuit thermodynamique, appelé aussi liquéfacteur, pour refroidir un gaz. Dans le liquéfacteur, un fluide est comprimé puis détendu pour produire du froid. Les températures obtenues sont bien inférieures à -160 °C. Pour éviter de fortes variations de températures, il est préférable que le liquéfacteur fonctionne en continu. Il est aussi possible d'arrêter le liquéfacteur mais pour préserver ses divers composants, il faut prévoir plusieurs heures pour un tel arrêt. De même, une mise en marche d'un liquéfacteur est une opération longue qui dure plusieurs heures.It is moreover also known to use an exchanger, or condenser, forming part of a thermodynamic circuit, also called a liquefier, to cool a gas. In the liquefier, a fluid is compressed and then expanded to produce cold. The temperatures obtained are well below -160 ° C. To avoid strong temperature variations, it is preferable for the liquefier to operate continuously. It is also possible to stop the liquefier, but to preserve its various components, it is necessary allow several hours for such a stop. Likewise, starting a liquefier is a long operation which lasts several hours.

Ainsi on a d'un côté un liquéfacteur qui produit du froid de préférence de manière continue et d'un autre côté une station de remplissage qui "consomme" le gaz naturel liquéfié produit grâce au liquéfacteur de manière fort irrégulière, en fonction de l'arrivée de citernes à remplir. Lorsque le débit de gaz naturel liquéfié sortant du réservoir de la station de remplissage est relativement important et que plusieurs citernes sont à remplir tous les jours, on peut alors adapter la production de froid du liquéfacteur pour satisfaire les besoins en gaz naturel liquéfié de la station de remplissage. Par contre, lorsque le débit de la station de remplissage est relativement faible, par exemple lorsqu'il arrive que pendant plus de vingt-quatre heures d'affilée aucun remplissage de citerne n'est à réaliser, la gestion entre la production de gaz liquéfié et le débit sortant est difficile à gérer.Thus we have on the one hand a liquefier which produces cold preferably continuously and on the other hand a filling station which "consumes" the liquefied natural gas produced thanks to the liquefier in a very irregular manner, depending on the arrival of tanks to fill. When the flow of liquefied natural gas leaving the tank of the filling station is relatively high and several tanks have to be filled every day, it is then possible to adapt the production of cold from the liquefier to meet the liquefied natural gas requirements of the station. filling. On the other hand, when the flow rate of the filling station is relatively low, for example when it happens that for more than twenty-four hours in a row no tank filling is to be carried out, the management between the production of liquefied gas and the outgoing flow is difficult to manage.

Pour de telles stations à débit irrégulier et/ou faible, il est parfois nécessaire d'arrêter la production de froid et donc le liquéfacteur. Les arrêts et remises en route sont alors gérés manuellement par un opérateur en charge de la gestion de la station de remplissage.For such stations with irregular and / or low flow, it is sometimes necessary to stop the production of cold and therefore the liquefier. Stops and restarts are then managed manually by an operator in charge of managing the filling station.

La présente invention a alors pour but de fournir une station de remplissage associée à un liquéfacteur pour lequel la production et le stockage de gaz (naturel) liquéfié soient réalisés automatiquement.The object of the present invention is therefore to provide a filling station associated with a liquefier for which the production and storage of liquefied (natural) gas are carried out automatically.

Un autre but de la présente invention est de fournir une telle station pouvant fonctionner sans avoir à arrêter le fonctionnement du liquéfacteur associé à la station de remplissage.Another object of the present invention is to provide such a station which can operate without having to stop the operation of the liquefier associated with the filling station.

À cet effet, la présente invention propose une station de remplissage de gaz liquéfié et de production de gaz liquéfié telle que définie par la revendication 1.To this end, the present invention provides a station for filling liquefied gas and producing liquefied gas as defined by claim 1.

Une station selon la présente invention peut produire automatiquement un gaz liquéfié grâce notamment à la mise en œuvre d'un liquéfacteur (second circuit avec son échangeur) dans lequel la pression du fluide frigorigène est modifiable et a une régulation originale basée, d'une part, sur le niveau dans le réservoir et sur la température du gaz liquéfié en un point entre l'échangeur et le réservoir et, d'autre part, sur une action sur la pression du fluide frigorigène dans le liquéfacteur. On associe de la sorte un système de production de gaz liquéfié proposant différents régimes de fonctionnement (avec de préférence un régime correspondant à un mode de fonctionnement ralenti) avec un système de régulation original permettant un fonctionnement automatisé.A station according to the present invention can automatically produce a liquefied gas thanks in particular to the implementation of a liquefier (second circuit with its exchanger) in which the pressure of the refrigerant is modifiable and has an original regulation based, on the one hand , on the level in the tank and on the temperature of the liquefied gas at a point between the exchanger and the tank and, on the other hand, on an action on the pressure of the refrigerant in the liquefier. In this way, a liquefied gas production system is associated with different operating regimes (preferably with a regime corresponding to an idle operating mode) with an original regulation system allowing automated operation.

Dans le second circuit d'une station de remplissage telle que décrite ci-dessus, des moyens peuvent aussi être prévus pour refroidir le fluide après sa compression et avant sa détente. On peut prévoir plusieurs cycles de compression et refroidissement, par exemple trois cycles successifs, suivis d'une détente.In the second circuit of a filling station as described above, means can also be provided for cooling the fluid after its compression and before its expansion. Several compression and cooling cycles can be provided, for example three successive cycles, followed by a relaxation.

L'agencement du second circuit est par exemple tel que celui-ci comporte en outre des moyens pour faire circuler son fluide réfrigérant dans l'échangeur après sa détente de son fluide réfrigérant et pour le ramener vers les moyens de compression de manière à réaliser un cycle fermé. Si plusieurs cycles compression, refroidissement et détente sont prévus, le fluide réfrigérant est de préférence amené après réchauffage dans l'échangeur de chaleur au premier étage de compression.The arrangement of the second circuit is for example such that it further comprises means for circulating its refrigerant fluid in the exchanger after its expansion of its refrigerant fluid and for returning it to the compression means so as to achieve a closed cycle. If several compression, cooling and expansion cycles are planned, the refrigerant fluid is preferably brought after reheating in the heat exchanger to the first compression stage.

Pour permettre la régulation de la pression dans le second circuit de fluide, ce dernier comporte par exemple un ballon de stockage de fluide présentant, d'une part, une entrée de fluide alimentée par une vanne pilotée disposée en aval des moyens permettant de comprimer le fluide et, d'autre part, une sortie de fluide commandée par une vanne pilotée permettant d'injecter du fluide contenu dans le ballon de stockage de fluide dans le second circuit en amont des moyens permettant de comprimer le fluide. Le second circuit peut alors être un circuit fermé.To allow the regulation of the pressure in the second fluid circuit, the latter comprises for example a fluid storage tank having, on the one hand, a fluid inlet supplied by a controlled valve arranged downstream of the means making it possible to compress the fluid. fluid and, on the other hand, a fluid outlet controlled by a controlled valve making it possible to inject the fluid contained in the fluid storage tank into the second circuit upstream of the means making it possible to compress the fluid. The second circuit can then be a closed circuit.

Le fluide utilisé dans le second circuit est avantageusement de l'azote qui est parfaitement adapté comme fluide frigorigène d'un circuit à pression modulable.The fluid used in the second circuit is advantageously nitrogen which is perfectly suited as refrigerant for a variable pressure circuit.

Le premier circuit comporte avantageusement une vanne de régulation de pression disposée en amont de l'échangeur. Cette vanne permet d'ajuster la pression du gaz dans le premier circuit afin d'éviter des surpressions. Elle permet également de couper l'arrivée de gaz, ce qui peut être nécessaire dans certaines conditions particulières.The first circuit advantageously comprises a pressure regulating valve arranged upstream of the exchanger. This valve makes it possible to adjust the gas pressure in the first circuit in order to avoid overpressures. It also cuts off the gas supply, which may be necessary in certain specific conditions.

Une forme de réalisation avantageuse de la présente invention prévoit que le système est tel que le premier circuit et le second circuit comportent un unique échangeur dans lequel circule dans un premier sens le fluide du second circuit après détente et dans un second sens, d'une part, le fluide du second circuit en aval des moyens permettant de comprimer le fluide et en amont des moyens de détente et, d'autre part, le gaz du premier circuit, ce gaz rentrant dans l'échangeur à l'état gazeux et en sortant à l'état liquide. Ceci permet de limiter le nombre de composants sans pour autant nuire aux performances du système dans son ensemble.An advantageous embodiment of the present invention provides that the system is such that the first circuit and the second circuit comprise a single exchanger in which the fluid of the second circuit circulates in a first direction after expansion and in a second direction, in a second direction. on the one hand, the fluid of the second circuit downstream of the means making it possible to compress the fluid and upstream of the expansion means and, on the other hand, the gas of the first circuit, this gas entering the exchanger in the gaseous state and in coming out in a liquid state. this allows the number of components to be limited without compromising the performance of the system as a whole.

Pour réguler un système selon l'invention, on prévoit par exemple que le système de commande et de gestion agit sur les moyens pour faire varier la pression dans le second circuit en fonction de la température mesurée par le dispositif de mesure de la température et en fonction du niveau de gaz liquéfié dans le réservoir.To regulate a system according to the invention, provision is made, for example, for the control and management system to act on the means for varying the pressure in the second circuit as a function of the temperature measured by the temperature measuring device and in depending on the level of liquefied gas in the tank.

Une variante de réalisation du système comporte une vanne pilotée disposée entre le dispositif de mesure de température et le réservoir. Dans cette variante de réalisation, on peut prévoir que pour la régulation dudit système, le système de commande et de gestion comporte une première boucle de contrôle par laquelle la vanne pilotée disposée entre le dispositif de mesure de température et le réservoir est contrôlée par le niveau de liquide dans le réservoir ainsi qu'une seconde boucle de contrôle par laquelle la pression dans le second circuit est contrôlée par la température mesurée par le dispositif de mesure de température.An alternative embodiment of the system comprises a piloted valve arranged between the temperature measuring device and the reservoir. In this variant embodiment, provision can be made for the regulation of said system, the control and management system to include a first control loop through which the piloted valve arranged between the temperature measuring device and the tank is controlled by the level. of liquid in the tank as well as a second control loop by which the pressure in the second circuit is controlled by the temperature measured by the temperature measuring device.

Des détails et avantages de la présente invention apparaitront mieux de la description qui suit, faite en référence au dessin schématique annexé sur lequel :

  • La figure 1 illustre schématiquement une première forme de réalisation de la présente invention, et
  • Les figures 2 à 4 sont des vues similaires à celle de la figure 1 pour des variantes de réalisation.
Details and advantages of the present invention will appear better from the following description, made with reference to the appended schematic drawing in which:
  • The figure 1 schematically illustrates a first embodiment of the present invention, and
  • The figures 2 to 4 are views similar to that of the figure 1 for variant embodiments.

On reconnaît sur la figure 1 (et sur les figures 2 à 4) un premier circuit 2 sur la droite et un second circuit 4 sur la gauche.We recognize on the figure 1 (and on figures 2 to 4 ) a first circuit 2 on the right and a second circuit 4 on the left.

Dans toute la description qui suit, le gaz circulant dans le premier circuit est du gaz naturel, à l'état gazeux ou liquide, et le fluide utilisé dans le second circuit est de l'azote (N2) qui reste à l'état gazeux. Toutefois, l'invention peut s'appliquer à un gaz liquéfié autre que du gaz naturel et le fluide frigorigène utilisé dans le second circuit peut être autre que de l'azote.Throughout the following description, the gas circulating in the first circuit is natural gas, in the gaseous or liquid state, and the fluid used in the second circuit is nitrogen (N 2 ) which remains in the state. gaseous. However, the invention can be applied to a liquefied gas other than natural gas and the refrigerant used in the second circuit can be other than nitrogen.

Le premier circuit présente une arrivée 6 de gaz naturel régulée en pression par une vanne de régulation de pression 8 destinée à alimenter un réservoir 10. Le gaz naturel arrive à l'état gazeux au niveau de l'arrivée 6 puis est liquéfié avant d'arriver dans le réservoir 10. Une pompe 12 est par exemple utilisée pour soutirer du gaz naturel liquéfié hors du réservoir 10 afin de remplir une citerne d'un camion citerne ou sur un bateau, un réservoir de bateau, ....The first circuit has a natural gas inlet 6 regulated in pressure by a pressure regulating valve 8 intended to supply a reservoir 10. The natural gas arrives in the gaseous state at the level of the inlet 6 then is liquefied before arriving in the reservoir 10. A pump 12 is for example used to draw liquefied natural gas out of the tank 10 in order to fill a tank of a tank truck or on a boat, a boat tank, ....

Le gaz au niveau de l'arrivée 6 est supposé être traité. S'il ne l'est pas, une unité de traitement (non représentée) qui réalise une purification du gaz par exemple par absorption ou de préférence par adsorption peut être prévue. Le gaz entrant dans le premier circuit 2 peut, à titre d'exemples illustratifs, provenir d'une canalisation ou bien d'une unité de production de bio-gaz ou digesteur.The gas at inlet 6 is assumed to be treated. If it is not, a treatment unit (not shown) which purifies the gas, for example by absorption or preferably by adsorption, can be provided. The gas entering the first circuit 2 can, by way of illustrative examples, come from a pipe or else from a biogas or digester production unit.

Le second circuit forme un système de compression et de détente combinés appelé par la suite liquéfacteur. Il comporte notamment un condenseur 14 en lien également avec le premier circuit et destiné à assurer la liquéfaction du gaz naturel dans ce circuit. On remarque également sur les figures 1 et 4 la présence d'un désurchauffeur 18 entre le premier circuit 2 et le second circuit 4. Ce désurchauffeur 18 permet un premier refroidissement du gaz naturel en provenance de l'arrivée 6 avant son introduction dans le condenseur 14 où il sera liquéfié puis stocké dans le réservoir 10. Le second circuit est ici un circuit fermé.The second circuit forms a combined compression and expansion system hereinafter called a liquefier. It comprises in particular a condenser 14 also linked to the first circuit and intended to ensure the liquefaction of natural gas in this circuit. We also notice on the figures 1 and 4 the presence of a desuperheater 18 between the first circuit 2 and the second circuit 4. This desuperheater 18 allows a first cooling of the natural gas coming from the inlet 6 before its introduction into the condenser 14 where it will be liquefied and then stored in the tank 10. The second circuit is here a closed circuit.

Dans le liquéfacteur, un moteur M entraine trois compresseurs C1, C2 et C3 formant chacun un étage d'une unité de compression. Pour la suite de la description du liquéfacteur, il est proposé de suivre de l'azote se déplaçant dans ce circuit.In the liquefier, a motor M drives three compressors C1, C2 and C3 each forming a stage of a compression unit. For the remainder of the description of the liquefier, it is proposed to monitor the nitrogen moving in this circuit.

L'azote arrive dans le compresseur C1 par une conduite R1 et en sort par une conduite R2. Il arrive alors à un premier refroidisseur 22 afin de réaliser un contrôle de la température de l'azote avant d'être renvoyé dans l'unité de compression par une conduite R3. L'azote est alors comprimé par le deuxième compresseur C2, puis amené par R4 à un deuxième refroidisseur 22 et d'atteindre par R5 un troisième étage de compression de l'unité de compression. Un troisième refroidisseur 22, relié au troisième compresseur C3 par une conduite R6, permet de contrôler la température de l'azote en sortie de l'unité de compression.The nitrogen arrives in the compressor C1 via a line R1 and leaves it via a line R2. It then arrives at a first cooler 22 in order to control the temperature of the nitrogen before being returned to the compression unit via a pipe R3. The nitrogen is then compressed by the second compressor C2, then brought through R4 to a second cooler 22 and through R5 to reach a third compression stage of the compression unit. A third cooler 22, connected to the third compressor C3 via an R6 pipe, allows the temperature of the nitrogen at the outlet of the compression unit to be controlled.

Une conduite R7 mène l'azote à un échangeur à contre courant 24 puis est amené par R8 à un détendeur 26. Ce dernier est mécaniquement lié au moteur M et à l'unité de compression. En sortie du détendeur 26, l'azote est alors amené (R9) vers le condenseur 14 où il absorbe des calories du gaz naturel que l'on souhaite liquéfier pour obtenir du gaz naturel liquéfié (LNG). En sortie du condenseur 14 l'azote est conduit (R10) vers le désurchauffeur 18 avant d'atteindre par R11 l'échangeur à contre courant 24 qui est relié en aval au premier compresseur C1 de l'unité de compression.A pipe R7 leads the nitrogen to a counter-current exchanger 24 then is supplied by R8 to a pressure reducing valve 26. The latter is mechanically linked to the engine M and to the compression unit. At the outlet of the expansion valve 26, the nitrogen is then brought (R9) to the condenser 14 where it absorbs calories from the natural gas that it is desired to liquefy in order to obtain liquefied natural gas (LNG). At the outlet of the condenser 14, the nitrogen is led (R10) to the desuperheater 18 before reaching through R11 the counter-current exchanger 24 which is connected downstream to the first compressor C1 of the compression unit.

On trouve également dans le second circuit 4 un ballon 28 de stockage d'azote qui est utilisé pour réguler la quantité d'azote dans le liquéfacteur, et donc la pression de cet azote dans le second circuit. Plus il y a d'azote dans le second circuit 4 (et donc moins il y a d'azote dans le ballon 28), plus la pression dans le second circuit 4 est élevée et plus le nombre de calories pouvant être prélevées au gaz naturel pour permettre sa liquéfaction est également élevé.There is also in the second circuit 4 a nitrogen storage tank 28 which is used to regulate the quantity of nitrogen in the liquefier, and therefore the pressure of this nitrogen in the second circuit. The more nitrogen there is in the second circuit 4 (and therefore the less nitrogen there is in the tank 28), the higher the pressure in the second circuit 4 and the greater the number of calories that can be taken from natural gas to allow its liquefaction is also high.

Pour remplir le ballon 28, on vient prélever de l'azote dans une partie du second circuit 4 où la pression est élevée, par exemple en sortie de l'unité de compression, de préférence après le dernier refroidisseur 22. Une vanne d'entrée 30 est utilisée pour réaliser un tel prélèvement.To fill the balloon 28, nitrogen is taken from a part of the second circuit 4 where the pressure is high, for example at the outlet of the compression unit, preferably after the last cooler 22. An inlet valve 30 is used to make such a sample.

De manière similaire, pour réintroduire de l'azote dans le second circuit 4, et donc vider partiellement (ou totalement) le ballon 28, une vanne de sortie 32 relie une sortie du ballon 28 à une portion du second circuit où la pression est basse, de préférence juste en amont de l'unité de compression et de son premier compresseur C1.Similarly, to reintroduce nitrogen into the second circuit 4, and therefore partially (or completely) empty the balloon 28, an outlet valve 32 connects an outlet of the balloon 28 to a portion of the second circuit where the pressure is low. , preferably just upstream of the compression unit and its first compressor C1.

Dans la forme de réalisation des figures 1 et 2, le premier circuit 2 comporte une vanne de remplissage 34 qui régule le flux de gaz naturel liquéfié rentrant dans le réservoir 10 et qui est disposée en amont du condenseur 14 et bien entendu en amont du réservoir 10.In the embodiment of figures 1 and 2 , the first circuit 2 comprises a filling valve 34 which regulates the flow of liquefied natural gas entering the reservoir 10 and which is arranged upstream of the condenser 14 and of course upstream of the reservoir 10.

La présente invention a pour but de réguler le remplissage du réservoir 10 en fonction des prélèvements réalisés dans ce réservoir par la pompe 12.The object of the present invention is to regulate the filling of the reservoir. 10 as a function of the samples taken from this reservoir by the pump 12.

À cet effet, la forme de réalisation des figures 1 et 2 prévoit de contrôler en continu le niveau de liquide dans le réservoir 10 et de mesurer la température en aval du condenseur 14. Le contrôle de niveau dans le réservoir 10 est réalisé par des capteurs LT connus de l'homme du métier et classiquement utilisés pour réaliser une mesure de niveau dans un réservoir de gaz naturel liquéfié. Ces capteurs LT sont reliés à un microcontrôleur LC qui traite l'information fournie par les capteurs LT.To this end, the embodiment of figures 1 and 2 provides for continuous monitoring of the liquid level in the tank 10 and for measuring the temperature downstream of the condenser 14. The level control in the tank 10 is performed by LT sensors known to those skilled in the art and conventionally used to achieve a level measurement in a liquefied natural gas reservoir. These LT sensors are connected to an LC microcontroller which processes the information supplied by the LT sensors.

Dans la forme de réalisation des figures 1 et 2, le microcontrôleur LC fournit également une commande en direction de la vanne de remplissage 34. On réalise ainsi une première boucle de contrôle dans la gestion du niveau de liquide dans le réservoir 10.In the embodiment of figures 1 and 2 , the LC microcontroller also provides a command in the direction of the filling valve 34. A first control loop is thus produced in the management of the liquid level in the reservoir 10.

La mesure de température est réalisée par un capteur TT qui est quant à lui relié à un microcontrôleur XC. Ce dernier, à partir de l'information concernant la température dans le premier circuit 2 en aval du condenseur agit sur la vanne d'entrée 30 et sur la vanne de sortie 32 pour adapter la quantité d'azote dans le second circuit 4. Lorsque la température mesurée par le capteur TT baisse, le microcontrôleur XC aura tendance, selon une loi de commande prédéterminée, à venir ouvrir la vanne d'entrée 30 afin de retirer de l'azote hors du second circuit 4. De ce fait l'absorption de calories dans le gaz naturel, et donc aussi la production de gaz naturel liquéfié, est limitée. De cette manière, une seconde boucle de contrôle est réalisée.The temperature measurement is performed by a TT sensor which is in turn connected to an XC microcontroller. The latter, from the information concerning the temperature in the first circuit 2 downstream of the condenser acts on the inlet valve 30 and on the outlet valve 32 to adapt the quantity of nitrogen in the second circuit 4. When the temperature measured by the TT sensor drops, the microcontroller XC will tend, according to a predetermined control law, to open the inlet valve 30 in order to withdraw nitrogen out of the second circuit 4. Therefore the absorption calories in natural gas, and therefore also the production of liquefied natural gas, is limited. In this way, a second control loop is realized.

Les deux boucles de contrôle sont liées. En effet, en agissant sur la vanne de remplissage 34, on fait varier la température mesurée par le capteur TT. Si à partir d'un régime continu d'écoulement de gaz naturel liquéfié du condenseur 14 vers le réservoir, la vanne de remplissage 34 s'ouvre, le gaz naturel liquéfié produit au niveau du condenseur 14 vient alors remplir le réservoir 10 plus rapidement et la température mesurée par le capteur TT s'élève. À l'inverse, si la vanne de remplissage 34 se ferme, le gaz naturel liquéfié a tendance à s'accumuler en amont du réservoir 10 et la température mesurée par le capteur TT va diminuer. Il y a donc ainsi une interaction physique entre les deux boucles de régulation.The two control loops are linked. In fact, by acting on the filling valve 34, the temperature measured by the sensor TT is varied. If from a continuous flow of liquefied natural gas from the condenser 14 to the tank, the filling valve 34 opens, the liquefied natural gas produced at the condenser 14 then fills the tank 10 more quickly and the temperature measured by the TT sensor rises. Conversely, if the filling valve 34 closes, the liquefied natural gas tends to accumulate upstream of the reservoir 10 and the temperature measured by the TT sensor will decrease. There is therefore an interaction physical between the two control loops.

Dans les variantes de réalisation des figures 3 et 4, on retrouve les capteurs de niveau LT et le microcontrôleur LC associé ainsi que le capteur de température TT. La valeur mesurée par le capteur de température est numérisée par un microcontrôleur TC et les informations obtenues par les capteurs de niveau et de température et traitées ensuite par les microcontrôleurs LC et TC sont collectées et analysées par le microcontrôleur XC qui est prévu pour agir sur la vanne d'entrée 30 et sur la vanne de sortie 32 du second circuit 4.In the alternative embodiments of figures 3 and 4 , we find the level sensors LT and the associated LC microcontroller as well as the temperature sensor TT. The value measured by the temperature sensor is digitized by a TC microcontroller and the information obtained by the level and temperature sensors and then processed by the LC and TC microcontrollers are collected and analyzed by the XC microcontroller which is intended to act on the inlet valve 30 and on the outlet valve 32 of the second circuit 4.

Dans cette forme de réalisation, la vanne de remplissage 34 prévue dans les variantes de réalisation des figures 1 et 2 peut être omise. La régulation présentée ici permet en effet de réguler aussi l'ensemble du système. L'analyse du niveau dans le réservoir permet de connaître la consommation de gaz naturel liquéfié et la mesure de la température en aval du condenseur 14. La seule régulation sur la pression de l'azote dans le second circuit permet de contrôler la production de gaz naturel liquéfié au sein du condenseur 14. En effet, la quantité de gaz liquéfié par le condenseur dépend des calories absorbées par le gaz entrant dans le premier circuit 2 par l'arrivée 6. En limitant la pression de l'azote dans le second circuit 4, on limite les calories absorbées au niveau du condenseur 14 (et éventuellement au niveau du désurchauffeur 18) et donc la production de gaz liquéfié.In this embodiment, the filling valve 34 provided in the alternative embodiments of the figures 1 and 2 can be omitted. The regulation presented here in fact also makes it possible to regulate the entire system. The analysis of the level in the tank makes it possible to know the consumption of liquefied natural gas and the measurement of the temperature downstream of the condenser 14. The only regulation on the pressure of the nitrogen in the second circuit makes it possible to control the gas production. natural liquefied within the condenser 14. In fact, the quantity of gas liquefied by the condenser depends on the calories absorbed by the gas entering the first circuit 2 through the inlet 6. By limiting the nitrogen pressure in the second circuit 4, the calories absorbed at the level of the condenser 14 (and possibly at the level of the desuperheater 18) and therefore the production of liquefied gas are limited.

Dans toutes les formes de réalisation, on remarque la présence aussi d'une boucle de contrôle en entrée du premier circuit 2. Cette régulation est une régulation habituelle sur une arrivée de gaz afin de réguler la pression dans le circuit et éviter des surpressions qui pourraient être dommageables. En outre, la régulation de cette pression permet d'ajuster la pression dans le condenseur à une valeur de consigne. Cette régulation peut aussi être utile par exemple lorsque le niveau dans le réservoir est haut et que l'on réduit la production de gaz naturel liquéfié, pour éviter de saturer le condenseur avec du gaz à l'état liquide.In all the embodiments, we also notice the presence of a control loop at the input of the first circuit 2. This regulation is a usual regulation on a gas inlet in order to regulate the pressure in the circuit and avoid overpressures which could. be damaging. In addition, the regulation of this pressure makes it possible to adjust the pressure in the condenser to a set value. This regulation can also be useful, for example, when the level in the reservoir is high and when the production of liquefied natural gas is reduced, to avoid saturating the condenser with gas in the liquid state.

Les variantes de réalisation des figures 2 et 3 prévoient de limiter le nombre d'échangeurs de chaleur et de regrouper le condenseur 14, le désurchauffeur 18 et l'échangeur à contre courant 24 par un unique échangeur/condenseur 114. Dans la forme de réalisation illustrée sur les figures 2 et 3, l'unique échangeur/condenseur 114 présente une voie centrale parcourue dans un sens et deux voies latérales parcourues à contresens. La voie centrale est empruntée par l'azote en sortie du détendeur 26 et avant son entrée dans l'unité de compression. Une voie latérale est empruntée par l'azote qui se refroidit après avoir été comprimé dans l'unité de compression et avant sa détente tandis que l'autre voie latérale est empruntée par le gaz qui rentre dans l'échangeur/condenseur 114 à l'état gazeux et en ressort à l'état liquide.The variants of figures 2 and 3 plan to limit the number of heat exchangers and to combine the condenser 14, the desuperheater 18 and the counter-current exchanger 24 by a single exchanger / condenser 114. In the embodiment illustrated in the figures 2 and 3 , the single exchanger / condenser 114 has a central lane traversed in one direction and two lateral lanes traversed in the opposite direction. The central path is taken by the nitrogen at the outlet of the pressure reducer 26 and before its entry into the compression unit. A lateral path is taken by the nitrogen which cools after having been compressed in the compression unit and before its expansion while the other lateral path is taken by the gas which enters the exchanger / condenser 114 at the gaseous state and emerges in the liquid state.

L'échangeur/condenseur 114 peut être par exemple un échangeur à plaques aluminium brasé. Le condenseur 14 et/ou l'échangeur à contre-courant 24 peuvent également être des échangeurs de ce type.The exchanger / condenser 114 may for example be a brazed aluminum plate exchanger. The condenser 14 and / or the countercurrent exchanger 24 can also be exchangers of this type.

Les différentes formes de réalisation décrites ci-dessus et illustrées sur le dessin annexé permettent de produire automatiquement et de stocker du gaz naturel liquéfié (ou un autre gaz liquéfié) sans avoir à mettre en marche et à arrêter le fonctionnement du liquéfacteur associé.The various embodiments described above and illustrated in the accompanying drawing make it possible to automatically produce and store liquefied natural gas (or another liquefied gas) without having to start and stop the operation of the associated liquefier.

Le cycle de réfrigération intègre un dispositif cryogénique d'expansion à l'azote qui peut être régulé en faisant varier la pression de l'azote dans le cycle. Les dispositifs de réfrigération correspondant permettent un fonctionnement au ralenti qui permet ici d'arrêter la production de gaz naturel liquéfié sans avoir à arrêter le cycle de réfrigération. Les composants du dispositif sont maintenus à température et peuvent ainsi de suite être utilisés pour passer en mode de production de gaz liquéfié.The refrigeration cycle incorporates a cryogenic nitrogen expansion device which can be regulated by varying the nitrogen pressure in the cycle. The corresponding refrigeration devices allow idling operation which here makes it possible to stop the production of liquefied natural gas without having to stop the refrigeration cycle. The components of the device are maintained at temperature and can thus be used to switch to liquefied gas production mode.

En mode de fonctionnement normal, du gaz naturel entre dans le système et est liquéfié puis stocké dans le réservoir. Une gestion du niveau dans le réservoir permet d'adapter la production de gaz naturel liquéfié aux besoins en gaz naturel liquéfié correspondant au débit de GNL hors du réservoir.During normal operation, natural gas enters the system and is liquefied and then stored in the tank. Management of the level in the reservoir makes it possible to adapt the production of liquefied natural gas to the needs of liquefied natural gas corresponding to the LNG flow rate out of the reservoir.

Bien entendu, la présente invention ne se limite pas aux formes de réalisation préférées décrites ci-dessus et illustrées sur le dessin à titre d'exemples non limitatifs. Elle concerne également toutes les variantes de réalisation à la portée de l'homme du métier dans le cadre des revendications ci-après.Of course, the present invention is not limited to the forms of preferred embodiment described above and illustrated in the drawing by way of non-limiting examples. It also relates to all the variant embodiments within the reach of a person skilled in the art within the framework of the claims below.

Claims (11)

  1. A liquefied gas filling station and liquefied gas production station, having:
    - a first circuit (2) with a liquefied gas tank (10) supplied with gas in the gaseous state by a gas supply line,
    - a second circuit (4) for coolant fluid fluidically independent of the first circuit with means making it possible to compress this fluid and to expand it, the second circuit (4) being a closed circuit, and
    - an exchanger (14, 114) for exchanging heat between the first circuit (2) and the second circuit (4), in which heat exchanger the fluid from the second circuit flows in a first direction after expansion of the fluid from the second circuit, and the gas from the first circuit flows in a second direction, this gas entering the exchanger in the gaseous state and leaving it in the liquid state, the heat exchange being performed upstream of the tank (10),
    characterized in that it further comprises:
    - means (LT) making it possible to determine the level of liquefied gas in the tank (10),
    - a device for measuring the temperature (TT) in the first circuit (2), downstream of the exchanger (14, 114) and upstream of the tank (10),
    - additional means (30, 32) for varying the pressure of the fluid within the second fluid circuit (4), and
    - a command and control system acting on the means (30, 32) to vary the pressure in the second circuit based on the temperature measured by the temperature measuring device and based on the level of liquefied gas in the tank.
  2. The filling station according to claim 1, characterized in that means (22) for cooling the fluid after its compression and before its expansion are provided in the second circuit (4).
  3. The filling station according to claim 2, characterized in that the second circuit comprises means (C1, C2, C3) making it possible to compress the coolant fluid and to cool it three times in succession and then to expand it.
  4. The filling station according to one of claims 1 to 3, characterized in that the second circuit further comprises means for circulating its coolant fluid in the exchanger (14, 114) after its expansion and for conveying it to the compression means (C1, C2, C3) so as to produce a closed cycle.
  5. The filling station according to one of claims 1 to 4, characterized in that the second fluid circuit (4) further comprises a fluid storage drum (28) having both a fluid inlet supplied by a pilot valve (30) arranged downstream of the means making it possible to compress the fluid and a fluid outlet controlled by a pilot valve (32) making it possible to inject fluid contained in the fluid storage drum (28) into the second circuit (4) upstream of the means making it possible to compress the fluid.
  6. The filing station according to one of claims 1 to 5, characterized in that the fluid used in the second circuit (4) is nitrogen.
  7. The filling station according to one of claims 1 to 6, characterized in that the first circuit (2) comprises a pressure regulating valve (8) arranged upstream of the exchanger (14, 114).
  8. The filling station according to one of claims 1 to 7, characterized in that the first circuit (2) and the second circuit (4) comprise a single exchanger (114) in which the fluid from the second circuit (4) flows in a first direction after expansion, and both the fluid from the second circuit (4) downstream of the means making it possible to compress the fluid and upstream of the expansion means, and the gas from the first circuit (2), flow in a second direction, this gas entering the exchanger (114) in the gaseous state and leaving it in the liquid state.
  9. The filling station according to one of claims 1 to 8, characterized in that the command and control system comprises a microcontroller (XC), and the microcontroller (XC) acts on the means (30, 32) to vary the pressure in the second circuit (4) based on the temperature measured by the temperature measuring device (TT) and based on the level of liquefied gas in the tank.
  10. The filling station according to one of claims 1 to 8, characterized in that it comprises a pilot valve (34) arranged between the temperature measuring device (TT) and the tank (10).
  11. The filling station according to claim 10, characterized in that the command and control system comprises a first control loop via which the pilot valve (34) arranged between the temperature measuring device (TT) and the tank (10) is controlled by the level of liquid in the tank (10) and also a second control loop via which the pressure in the second circuit (4) is controlled by the temperature measured by the temperature measuring device (TT).
EP14790184.7A 2013-08-21 2014-08-06 Liquefied gas filling station combined with a liquefied gas production device Active EP3036471B1 (en)

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FR1358107A FR3009858B1 (en) 2013-08-21 2013-08-21 LIQUEFIED GAS FILLING STATION ASSOCIATED WITH A DEVICE FOR THE PRODUCTION OF LIQUEFIED GAS
PCT/FR2014/052052 WO2015025096A2 (en) 2013-08-21 2014-08-06 Liquefied gas filling station combined with a liquefied gas production device

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FR3021091B1 (en) * 2014-05-14 2017-09-15 Ereie - Energy Res Innovation Eng METHOD AND DEVICE FOR LIQUEFACTING METHANE
FR3067092B1 (en) * 2017-05-31 2020-08-14 L'air Liquide Sa Pour L'etude Et L'exploitation Des Procedes Georges Claude STATION AND METHOD FOR FILLING A PRESSURIZED GAS TANK (S)
US10590835B2 (en) * 2017-07-31 2020-03-17 ESS Engineering A/S Supercharger
FR3086993B1 (en) * 2018-10-09 2021-11-26 Air Liquide PROCESS AND INSTALLATION FOR STORAGE AND DISTRIBUTION OF LIQUEFIED HYDROGEN
FR3098274B1 (en) * 2019-07-03 2022-01-28 Air Liquide Device and method for filling reservoirs.
WO2021254597A1 (en) * 2020-06-16 2021-12-23 Wärtsilä Finland Oy A system for producing liquefied product gas and method of operating the same

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US20160208984A1 (en) 2016-07-21
EP3036471A2 (en) 2016-06-29
CN105612381A (en) 2016-05-25
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FR3009858B1 (en) 2015-09-25
WO2015025096A3 (en) 2015-04-16

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