EP3026323A1 - Natural gas recovery system and vehicle comprising said system - Google Patents

Natural gas recovery system and vehicle comprising said system Download PDF

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Publication number
EP3026323A1
EP3026323A1 EP15194172.1A EP15194172A EP3026323A1 EP 3026323 A1 EP3026323 A1 EP 3026323A1 EP 15194172 A EP15194172 A EP 15194172A EP 3026323 A1 EP3026323 A1 EP 3026323A1
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EP
European Patent Office
Prior art keywords
tank
natural gas
gaseous phase
compressor
liquefied natural
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.)
Granted
Application number
EP15194172.1A
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German (de)
French (fr)
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EP3026323B1 (en
Inventor
Salvatore Basile
Clino D'Epiro
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Iveco SpA
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Iveco SpA
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Publication date
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Priority to EP19187952.7A priority Critical patent/EP3614035B1/en
Publication of EP3026323A1 publication Critical patent/EP3026323A1/en
Application granted granted Critical
Publication of EP3026323B1 publication Critical patent/EP3026323B1/en
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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
    • F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under 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
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/01—Mounting arrangements
    • F17C2205/0123—Mounting arrangements characterised by number of vessels
    • F17C2205/013—Two or more vessels
    • F17C2205/0134—Two or more vessels characterised by the presence of fluid connection between vessels
    • 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
    • F17C2205/0332—Safety valves or pressure relief valves
    • 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
    • F17C2205/0335—Check-valves or non-return valves
    • 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
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/03—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the pressure level
    • F17C2223/033—Small pressure, e.g. for liquefied gas
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2225/00—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel
    • F17C2225/01—Handled fluid after transfer, i.e. state of fluid after transfer from the vessel characterised by the phase
    • F17C2225/0146—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
    • 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
    • F17C2227/0157—Compressors
    • 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
    • F17C2250/01—Intermediate tanks
    • 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
    • F17C2250/03—Control means
    • F17C2250/032—Control means using computers
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04—Indicating or measuring of parameters as input values
    • F17C2250/0404—Parameters indicated or measured
    • F17C2250/043—Pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04—Indicating or measuring of parameters as input values
    • F17C2250/0404—Parameters indicated or measured
    • F17C2250/0439—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
    • F17C2265/00—Effects achieved by gas storage or gas handling
    • F17C2265/03—Treating the boil-off
    • F17C2265/032—Treating the boil-off by recovery
    • F17C2265/037—Treating the boil-off by recovery with pressurising
    • 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
    • F17C2265/066—Fluid distribution for feeding engines for propulsion
    • 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
    • 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
    • F17C2270/0184—Fuel cells

Definitions

  • the present invention relates to the field of natural gas systems for vehicles and in particular to liquefied natural gas systems.
  • a tank adapted to store LNG tends to release towards the atmosphere a certain amount of gas which depends on the pressure and temperature of the gas in the tank. In general it is estimated that after about 180h the first releases of gases to the outside occur.
  • Such gas contributes to the calculation of the emissions of a vehicle, since natural gas is a greenhouse gas similar to carbon dioxide.
  • the purpose of the present invention is to reduce the overall emissions of a vehicle fuelled with liquefied natural gas.
  • the basic idea of the present invention is to recover the natural gas released from the liquefied natural gas tank and to store it in another appropriate tank.
  • this appropriate tank is a high pressure tank for compressed natural gas.
  • a first conventional tank for liquefied natural gas is joined by a second tank for compressed natural gas.
  • a pressure sensor is present in the first tank and when it measures a pressure higher than a predefined threshold, a processing unit orders the activation of a compressor having an inlet communicating with the first tank and an outlet communicating with the second tank, in order to remove the excess gas from the first tank and compress it in the second tank.
  • the first tank comprises a safety valve calibrated at a pressure greater than the activation pressure of the aforesaid predefined pressure threshold, so that, in case of malfunction of any component of the recovery system, the excess gas can be released into the environment without any risk.
  • a check valve or a solenoid valve controlled by the processing unit is housed on the inlet or the outlet of the compressor.
  • the first tank is connected to the second tank through an expansion chamber and a compressor in succession.
  • the compressor therefore has an inlet in communication with the expansion chamber and an outlet in communication with the second tank.
  • the connection between the first tank and the expansion chamber is made by means of a first safety/overpressure valve which releases the excess gas of the first tank into the expansion chamber.
  • the expansion chamber contains a pressure sensor. When it measures a pressure above a predefined threshold inside the expansion chamber, a processing unit orders the activation of the compressor which withdraws the gas released in the expansion chamber and compresses it in the second tank.
  • the first tank and/or the expansion chamber comprises a second safety valve calibrated at a pressure greater than the activation pressure of the first safety/overpressure valve, so that, in case of malfunction of any component of the recovery system, the excess gas can be released into the environment without any risk.
  • This second variant compared to the first, makes it possible to do without the pressure sensor in the first tank, where temperatures are below -100°C. In addition, it makes it possible to avoid modifying a tank for liquefied natural gas, keeping it as originally conceived.
  • the recovered gas can be used to drive the vehicle resulting in a corresponding increase of total mileage, with undoubted economic and environmental advantages.
  • the present invention relates to a system for the recovery of natural gas released from a liquefied natural gas tank, as described in claim 1.
  • Another object of the present invention is a natural gas supply system comprising the aforesaid recovery system.
  • a further object of the present invention is a land vehicle fitted with an internal combustion engine powered by a liquefied natural gas fuel supply system comprising the aforesaid recovery system.
  • second component does not imply the presence of a “first” component.
  • Figure 1 shows a first preferred variant of the present invention wherein a first tank 1 is of the type intended to store liquefied natural gas.
  • a first safety valve V1 places the tank 1 in communication with the environment. Generally, this valve is connected to a first opening placed in the upper part of the tank, so as to intercept only the gaseous phase.
  • a second opening H2, different from the first opening, is connected to an inlet of a compressor CP.
  • the outlet of the compressor CP is connected to a second tank 2 intended to store compressed natural gas.
  • a check valve CV is placed upstream or downstream of the compressor CP, depending on the direction of circulation of the gas aspirated from the tank 1 and introduced into the tank 2.
  • a pressure sensor P is housed in the first tank 1.
  • a CPU processing unit is connected to said pressure sensor P and when the pressure measured by it exceeds a predefined threshold, the processing unit orders the activation of the compressor which aspirates natural gas in the gaseous phase from the first tank 1 compressing it in the second tank 2.
  • said predefined threshold is appropriately below an activation threshold of the first safety valve V1.
  • Both the first tank and the second tank comprise respective openings towards the injection device of the natural gas supply system fuelling the internal vehicular combustion engine, not shown.
  • FIG. 2 shows another preferred variant of the invention in which the first and second tank are present, as in the previous example.
  • the connection between the first tank is made in succession through an expansion chamber EX and the compressor CP.
  • the first tank as before, comprises a first safety valve V1 which places the tank 1 in communication with the environment.
  • the first tank comprises a second safety /overpressure valve V2 which connects the first tank with the expansion chamber EX.
  • the compressor CP has an inlet connected with the expansion chamber EX and an outlet connected with the second tank 2.
  • a check valve CV is placed between the expansion chamber EX and the compressor CP, or downstream of it, i.e. between the compressor CP and the second tank 2.
  • a pressure sensor P is housed in the expansion chamber EX.
  • a CPU processing unit is connected to said pressure sensor P and when the pressure measured by it exceeds a predefined threshold, the processing unit orders the activation of the compressor which aspirates natural gas in the gaseous phase from the expansion chamber compressing it in the second tank 2.
  • the pressure thresholds that determine both the opening of the overpressure/safety valve V2 and the activation of the compressor are appropriately below an activation threshold of the first safety valve V1.
  • the compressor CP is preferably an electro-compressor.
  • the second tank too may be fitted with a safety valve not shown.
  • a pressure sensor is completely optional, as it is possible to estimate the excess gaseous phase in the first tank in different ways, for example on the basis of the quantity and temperature of the liquid phase present in the first tank.
  • the quantity may be determined indirectly based on the capacity of the first tank 1 based on the consumption of liquefied natural gas.
  • Embodiment variants may be made to the non-limiting example described, while remaining within the scope of protection of the present invention, comprising all the equivalent embodiments for a person skilled in the art.

Abstract

A natural gas recovery system for a liquefied natural gas vehicular supply system, the vehicular supply system comprising a first tank (1), intended to store liquefied natural gas, a liquid phase and a gaseous phase of said natural gas coexisting in the first tank, the recovery system of natural gas comprising a second tank (2) intended to store compressed natural gas, a compressor (CP), adapted to compress in the second tank (2) an excess gaseous phase of the first tank.

Description

    Field of application of the invention
  • The present invention relates to the field of natural gas systems for vehicles and in particular to liquefied natural gas systems.
    • State of the art
  • A tank adapted to store LNG (Liquefied Natural Gas), tends to release towards the atmosphere a certain amount of gas which depends on the pressure and temperature of the gas in the tank. In general it is estimated that after about 180h the first releases of gases to the outside occur.
  • This happens mainly for safety reasons, in that, over time, the gaseous phase in the tank tends to increase, resulting in an increase in pressure. Therefore, in order to prevent the pressures from exceeding given values, the excess gaseous phase is released into the environment.
  • Such gas contributes to the calculation of the emissions of a vehicle, since natural gas is a greenhouse gas similar to carbon dioxide.
    • Summary of the invention
  • The purpose of the present invention is to reduce the overall emissions of a vehicle fuelled with liquefied natural gas.
  • The basic idea of the present invention is to recover the natural gas released from the liquefied natural gas tank and to store it in another appropriate tank.
  • Preferably, this appropriate tank is a high pressure tank for compressed natural gas. As a result, a first conventional tank for liquefied natural gas is joined by a second tank for compressed natural gas.
  • According to a first preferred variant of the invention, a pressure sensor is present in the first tank and when it measures a pressure higher than a predefined threshold, a processing unit orders the activation of a compressor having an inlet communicating with the first tank and an outlet communicating with the second tank, in order to remove the excess gas from the first tank and compress it in the second tank.
  • Preferably, the first tank comprises a safety valve calibrated at a pressure greater than the activation pressure of the aforesaid predefined pressure threshold, so that, in case of malfunction of any component of the recovery system, the excess gas can be released into the environment without any risk.
  • Preferably, a check valve or a solenoid valve controlled by the processing unit is housed on the inlet or the outlet of the compressor.
  • According to another preferred variant of the invention, the first tank is connected to the second tank through an expansion chamber and a compressor in succession. The compressor therefore has an inlet in communication with the expansion chamber and an outlet in communication with the second tank. The connection between the first tank and the expansion chamber is made by means of a first safety/overpressure valve which releases the excess gas of the first tank into the expansion chamber. The expansion chamber contains a pressure sensor. When it measures a pressure above a predefined threshold inside the expansion chamber, a processing unit orders the activation of the compressor which withdraws the gas released in the expansion chamber and compresses it in the second tank.
  • Preferably, the first tank and/or the expansion chamber comprises a second safety valve calibrated at a pressure greater than the activation pressure of the first safety/overpressure valve, so that, in case of malfunction of any component of the recovery system, the excess gas can be released into the environment without any risk.
  • This second variant, compared to the first, makes it possible to do without the pressure sensor in the first tank, where temperatures are below -100°C. In addition, it makes it possible to avoid modifying a tank for liquefied natural gas, keeping it as originally conceived.
  • Advantageously, the recovered gas can be used to drive the vehicle resulting in a corresponding increase of total mileage, with undoubted economic and environmental advantages.
  • The present invention relates to a system for the recovery of natural gas released from a liquefied natural gas tank, as described in claim 1.
  • Another object of the present invention is a natural gas supply system comprising the aforesaid recovery system.
  • A further object of the present invention is a land vehicle fitted with an internal combustion engine powered by a liquefied natural gas fuel supply system comprising the aforesaid recovery system.
  • The claims describe preferred variants of the invention forming an integral part of the present description.
    • Brief description of the figures
  • Further purposes and advantages of the present invention will be clear from the detailed description below of an example of embodiment thereof (and of its variants) and the appended drawings provided merely by way of a non-limiting example, wherein:
    • Figure 1 shows a diagram of a first variant of the present invention,
    • Figure 2 shows a diagram of a second variant of the present invention,
  • Identical reference numerals and letters in the drawings refer to the same elements or components.
  • The features shown in the drawings may be considered independently of one another.
  • In the present description the term "second" component does not imply the presence of a "first" component. These terms are in fact used only for clarity and are not intended as limiting.
    • Detailed description of embodiments
  • Figure 1 shows a first preferred variant of the present invention wherein a first tank 1 is of the type intended to store liquefied natural gas.
  • Introduced into the tank 1 at very low temperature, about - 120°C, over time it tends to gasify, so that a liquid phase L and a gaseous phase G are identified in the tank.
  • A first safety valve V1 places the tank 1 in communication with the environment. Generally, this valve is connected to a first opening placed in the upper part of the tank, so as to intercept only the gaseous phase.
  • A second opening H2, different from the first opening, is connected to an inlet of a compressor CP. The outlet of the compressor CP is connected to a second tank 2 intended to store compressed natural gas.
  • Consequently the safety valve V1 and the hydraulic line connecting the first tank 1 with the second tank 2 are independent of each other, see figures 1 and 2.
  • A check valve CV is placed upstream or downstream of the compressor CP, depending on the direction of circulation of the gas aspirated from the tank 1 and introduced into the tank 2.
  • A pressure sensor P is housed in the first tank 1.
    A CPU processing unit is connected to said pressure sensor P and when the pressure measured by it exceeds a predefined threshold, the processing unit orders the activation of the compressor which aspirates natural gas in the gaseous phase from the first tank 1 compressing it in the second tank 2. Clearly, said predefined threshold is appropriately below an activation threshold of the first safety valve V1.
  • Both the first tank and the second tank comprise respective openings towards the injection device of the natural gas supply system fuelling the internal vehicular combustion engine, not shown.
  • The English term "to the engine" indicates said operational connection between the tanks 1 and 2 and the internal combustion engine.
  • Figure 2 shows another preferred variant of the invention in which the first and second tank are present, as in the previous example.
  • The connection between the first tank is made in succession through an expansion chamber EX and the compressor CP.
    The first tank, as before, comprises a first safety valve V1 which places the tank 1 in communication with the environment. In addition, the first tank comprises a second safety /overpressure valve V2 which connects the first tank with the expansion chamber EX.
  • The compressor CP has an inlet connected with the expansion chamber EX and an outlet connected with the second tank 2. A check valve CV is placed between the expansion chamber EX and the compressor CP, or downstream of it, i.e. between the compressor CP and the second tank 2.
  • A pressure sensor P is housed in the expansion chamber EX.
    A CPU processing unit is connected to said pressure sensor P and when the pressure measured by it exceeds a predefined threshold, the processing unit orders the activation of the compressor which aspirates natural gas in the gaseous phase from the expansion chamber compressing it in the second tank 2.
  • Clearly, the pressure thresholds that determine both the opening of the overpressure/safety valve V2 and the activation of the compressor are appropriately below an activation threshold of the first safety valve V1.
  • The compressor CP is preferably an electro-compressor.
    For both examples, it may be advantageous to introduce a second pressure sensor inside the second tank, so as to inhibit the activation of the electro-compressor when the pressure measured in the second tank exceeds a further predefined threshold.
  • This avoids having to activate the compressor unnecessarily, which if electric would consume electricity without any real benefit to the system or which could lead to excessive pressure in the second tank.
  • The second tank too, for safety reasons, may be fitted with a safety valve not shown.
  • It is worth pointing out that the implementation of a pressure sensor is completely optional, as it is possible to estimate the excess gaseous phase in the first tank in different ways, for example on the basis of the quantity and temperature of the liquid phase present in the first tank.
  • The quantity may be determined indirectly based on the capacity of the first tank 1 based on the consumption of liquefied natural gas.
  • Other rough estimates may be made by knowing the time elapsed since refuelling, the environmental temperature, the capacity of the tank 1 and the amount of liquefied natural gas consumed.
  • Embodiment variants may be made to the non-limiting example described, while remaining within the scope of protection of the present invention, comprising all the equivalent embodiments for a person skilled in the art.
  • From the above description a person skilled in the art may make the object of the invention without introducing any further construction details. The elements and features shown in the various preferred embodiments may be combined while remaining within the scope of protection of the present application All the characteristics described in the description of the state of the art, unless specifically contested or excluded in the detailed description, should be considered in combination with the features of the variants described in the detailed description, forming an integral part of the present invention.

Claims (15)

  1. A natural gas recovery system for a liquefied natural gas vehicular supply system, the vehicular supply system comprising a first tank (1), intended to store liquefied natural gas, a liquid phase and a gaseous phase of said natural gas coexisting in the first tank,
    the recovery system of natural gas comprising a second tank (2) intended to store compressed natural gas, a compressor (CP), adapted to compress in said second tank (2) an excess of gaseous phase of said first tank.
  2. The system according to claim 1, wherein said compressor has an inlet operatively connected with said first tank (1) and an outlet operatively connected with said second tank (2).
  3. The system according to claim 1, further comprising an expansion chamber (EX) operatively connected with said first tank (1) and wherein said compressor has an inlet operatively connected with said expansion chamber (EX) and an outlet operatively connected with said second tank (2).
  4. The system according to any one of the previous claims, further comprising estimation means (P, CPU) of said excess gaseous phase and processing means configured to activate said compressor (CP) coherently with said excess of gaseous phase estimation.
  5. The system according to claim 4, wherein said estimation means of said excess gaseous phase comprise a pressure sensor (P), and wherein said pressure sensor (P) is installed in said first tank (1) or, if said expansion chamber (EX) is provided, in said expansion chamber (EX).
  6. The system according to any one of the previous claims, wherein said first tank (1) comprises a first safety valve (VI) adapted to place in communication said first tank (1) with the environment, when a pressure inside said first tank (1) exceeds a first predefined pressure threshold and wherein said first safety valve is connected to said first tank independently of an interconnection between said first and second tank.
  7. The system according to claim 6, wherein, when said expansion chamber (EX) is provided, it is operatively connected to said first tank (1) by means of an overpressure valve (VI) calibrated at an opening pressure value lower than said first predefined pressure threshold.
  8. The system according to claim 5, wherein said tank comprises a first safety valve (VI) adapted to place in communication said first tank (1) with the environment when a first predefined pressure threshold is exceeded and wherein said processing means (CPU) are configured to activate said compressor (CP) when a pressure measured by said pressure sensor (P) exceeds a second predefined pressure threshold lower than said first predefined pressure threshold.
  9. The system according to any one of the previous claims, further comprising a check valve arranged between said compressor (CP) and said second tank.
  10. A liquefied natural gas vehicular supply system comprising a first tank (1) intended to store liquefied natural gas, a liquid phase and a gaseous phase of said natural gas coexisting in the first tank, and comprising a recovery system of natural gas according to any one of the previous claims.
  11. The system according to claim 10, comprising means for withdrawing liquefied natural gas from said first tank (1) and compressed natural gas from said second tank (2).
  12. A land vehicle equipped with an internal combustion engine supplied by a liquefied natural gas supply system according to one of claims 10 or 11.
  13. A method of recovery of natural gas from a liquefied natural gas vehicular supply system, the vehicular supply system comprising a first tank (1), intended to store liquefied natural gas, a liquid phase and a gaseous phase of said natural gas coexisting in the first tank,
    the method comprising a step of recovering an excess gaseous phase of said first tank (1) and compressing it in a second tank (2).
  14. The method according to claim 13, wherein said step is performed progressively as said excess gaseous phase forms.
  15. The method according to one of claims 13 or 14, further comprising a step of adopting said liquefied natural gas and said compressed natural gas to supply an internal combustion engine.
EP15194172.1A 2014-11-11 2015-11-11 Natural gas recovery system and vehicle comprising said system Active EP3026323B1 (en)

Priority Applications (1)

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ITTO20140937 2014-11-11

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Cited By (1)

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Publication number Priority date Publication date Assignee Title
WO2018015640A1 (en) * 2016-07-21 2018-01-25 Engie Module and system for depressurising a cryogenic tank

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Publication number Priority date Publication date Assignee Title
US5540208A (en) * 1994-09-13 1996-07-30 Nabco Limited Liquefied gas fuel supply system
EP1838991A1 (en) * 2005-01-21 2007-10-03 Cryostar SAS Natural gas supply method and apparatus
DE202013101593U1 (en) * 2013-04-15 2013-04-24 EES-Autogas Technologiezentrum UG (haftungsbeschränkt) Device for gas supply
WO2014006265A1 (en) * 2012-07-03 2014-01-09 Lngtainer Ab Tank
DE102012024717A1 (en) * 2012-12-18 2014-06-18 Daimler Ag Vehicle has liquefied petroleum gas tank for accommodating liquefied petroleum gas as fuel for internal combustion engine of vehicle and overpressure discharge line for discharging vaporized gas, which is connected with gas tank

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5540208A (en) * 1994-09-13 1996-07-30 Nabco Limited Liquefied gas fuel supply system
EP1838991A1 (en) * 2005-01-21 2007-10-03 Cryostar SAS Natural gas supply method and apparatus
WO2014006265A1 (en) * 2012-07-03 2014-01-09 Lngtainer Ab Tank
DE102012024717A1 (en) * 2012-12-18 2014-06-18 Daimler Ag Vehicle has liquefied petroleum gas tank for accommodating liquefied petroleum gas as fuel for internal combustion engine of vehicle and overpressure discharge line for discharging vaporized gas, which is connected with gas tank
DE202013101593U1 (en) * 2013-04-15 2013-04-24 EES-Autogas Technologiezentrum UG (haftungsbeschränkt) Device for gas supply

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018015640A1 (en) * 2016-07-21 2018-01-25 Engie Module and system for depressurising a cryogenic tank
FR3054286A1 (en) * 2016-07-21 2018-01-26 Engie MODULE AND SYSTEM FOR DEPRESSURIZING A CRYOGENIC RESERVOIR
CN109563966A (en) * 2016-07-21 2019-04-02 能源集团 Module and system for being depressurized to cryogenic tank
US11353161B2 (en) 2016-07-21 2022-06-07 Engie Module and system for depressurising a cryogenic tank

Also Published As

Publication number Publication date
EP3614035A1 (en) 2020-02-26
ES2754232T3 (en) 2020-04-16
EP3026323B1 (en) 2019-08-14
EP3614035B1 (en) 2022-12-28
ES2939463T3 (en) 2023-04-24

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