AERONAUTICAL GAS DISTRIBUTION DEVICE

Abstract

Aeronautical device 1 for distributing gas in an aircraft between at least one source 2 of liquefied gas and at least one gas consumer member 3, comprising at least one first controlled all-or-nothing valve 11 at the output of each source 2 of liquefied gas, a cryogenic distributor 5 connected to each first controlled valve 11 and supplied with liquid, second controlled all-or-nothing valves 12 connected to the cryogenic distributor 5, in parallel, two-phase buffer reservoirs 7 supplied with liquid, each via one of the second controlled valves, and supplying gas, third controlled valves 13 mounted at the output of each buffer reservoir 7, for supplying gas, a pressure-reducing valve 9 mounted at the output of the third controlled valves 13, a collector 10 supplied by the pressure-reducing valve 9 in order to supply the at least one consumer member 3.

Description

AERONAUTICAL GAS DISTRIBUTION DEVICE

[0001] The present invention relates to the field of aeronautics.

[0002] Since its inception, aviation has used high-octane gasoline engines. After 1945, the development of jet engines and turbines led to the use of kerosene, which has a higher molecular weight than gasoline, a higher energy density, higher efficiency, and lower flammability. These fuels are generally stored in tanks located in the wings, in the fuselage-wing connection, or in the tail.

[0003] The trend toward reducing carbon dioxide emissions has led to more fuel-efficient engines. However, the gains in carbon dioxide emissions are diminishing as certain technologies mature, particularly blade tip speeds. It has become increasingly desirable to introduce a breakthrough.

[0004] This is how gas-powered aircraft projects emerged. Combustion of short-chain or non-existent carbon gases, possibly with oxygen, is low-polluting or non-polluting. However, the storage of H2, O2, or C1 or C2 gases, due to the small size of the gas molecule, is difficult and subject to leak risks.

[0005] On the ground, the storage of hydrogen, methane, ethane, ethylene, acetylene or oxygen is generally carried out in pressurized envelopes that are too heavy, too bulky and contain too much pressure potential energy to be carried on board an aircraft or in welded and / or glued cryogenic tanks. Cryogenic storage is limited to a limited duration proportional to the volume stored.

[0006] Furthermore, gas stored in liquid state cannot be used by an internal or external combustion engine or a fuel cell. Final consumption requires gas within a temperature and pressure range specified by the manufacturer of the consumer unit.

[0007] The need arose to package gas within an aircraft for on-board consumption.

[0008] The invention proposes an aeronautical device for distributing gas in an aircraft between at least one source of liquefied gas and at least one gas consuming member. The device comprises at least one first, all-or-nothing, controlled valve at the outlet of each source of liquefied gas, a cryogenic distributor connected to each first controlled valve and supplied with liquid, second, all-or-nothing, controlled valves connected to the cryogenic distributor, in parallel, two-phase buffer tanks, supplied with liquid, each by one of said second controlled valves, and supplying gas, third controlled valves, mounted at the outlet of each buffer tank, to supply gas, a pressure regulator mounted at the outlet of the third controlled valves, and a manifold supplied by the pressure regulator to supply said at least one consuming member.Thanks to the invention, the aeronautical gas distribution device can provide the aircraft, through the volume contained in the buffer tanks, with the necessary autonomy regardless of the state of the liquefied gas source. The buffer tanks can be designed for a gas pressure of several hundred bars, a chosen gas pressure nevertheless being supplied to the consuming organs.

[0009] Unlike in the space sector, where a cryogenic valve is used once and does not need to be closed again, reclosable valves, such as solenoid valves, are provided.

[0010] In one embodiment, the device comprises fourth controlled valves mounted at the outlet of each regulator, to supply gas. The consuming organ(s), for example the thrusters or an auxiliary for generating electrical energy on board, can be supplied from just one of the buffer tanks, any one.

[0011] In one embodiment, the device comprises at least one compressor powered by at least one of the buffer tanks, and at least one fifth controlled valve mounted between the compressor and said buffer tank. The buffer tank can be emptied sufficiently so as to increase the quantity of gas available for the consuming organs and bring the buffer tank to a pressure at the end of emptying lower than the current pressure in the cryogenic tank designated at that time for filling. The current pressure in the cryogenic tank is equal to the pressure in the distributor when the The first corresponding valve is opened and, if applicable, the other first valves closed. The buffer tank is then filled with gas by operating a cryogenic valve under the effect of the pressure difference. Doing without a cryogenic pump saves weight and reduces the risk of incidents.

[0012] In one embodiment, the device comprises a control unit controlling the at least one first controlled valve for sequential filling of the buffer tanks by pressure difference and sequential emptying of the buffer tanks. The sequential operation makes it possible to make the number of cryogenic tanks and the number of buffer tanks independent. At least one cryogenic tank is provided. At least two, preferably three, buffer tanks are provided.

[0013] In the case of two buffer tanks, one is being emptied while the other is being filled or gasified by heating the gas.

[0014] In the case of three or more buffer tanks, one is being emptied while a second is being filled and a third is being gasified by heating the gas or already filled with gas to the planned pressure. The gasification requires a duration depending on the quantity of liquid brought into the buffer tank, the outside temperature which may range from -55°C at altitude to +60°C on the ground and the speed of the aircraft, in particular. The duration of gasification and the quantity of liquid admitted into the buffer tank can be estimated.

[0015] During gasification, if the corresponding buffer tank exceeds a maximum pressure, then the control unit can command a switching to discharge the overpressure buffer tank and momentarily interrupt the emptying of another buffer tank, then resume the operation prior to the detected overpressure.

[0016] In one embodiment, for emptying one of the buffer tanks, the control unit controls the third valves controlled for a gas flow by pressure difference in a first step, then by actuation of a compressor in a second step until a pressure in said buffer tank lower than the pressure existing in the cryogenic distributor. The operation of the compressor is limited in time, thus saving energy.

[0017] In one embodiment, the at least one first valve and the second valves are cryogenic. The other valves are passed through by gas at a lower temperature, for example approximately -55°C at altitude.

[0018] In one embodiment, the device comprises a flow meter arranged at the outlet of each source of liquefied gas. The measurement of the liquid flow rate makes it possible to manage the opening time of the first and second valves and the distribution device to supply a requested quantity.

[0019] In one embodiment, additional flow meters are advantageously arranged at the inlet of the buffer tanks.

[0020] In one embodiment, an assembly comprises a device described above and at least one single cryogenic source of liquefied gas. One of the cryogenic tanks may be being drained to fill a buffer tank while the other cryogenic tank(s) are inactive. In the event of overpressure in a cryogenic tank, priority draining to the distribution device may be provided.

[0021] In one embodiment, the aeronautical method for distributing gas in an aircraft between at least one source of liquefied gas and at least one gas-consuming member, comprises a step of filling a buffer tank with liquefied gas by at least one of at least one first, all-or-nothing, controlled valve at the outlet of each source of liquefied gas, a cryogenic distributor connected to each first controlled valve, supplied with liquid by the cryogenic distributor, one of the second, all-or-nothing, controlled valves connected to the cryogenic distributor in parallel, said buffer tank being connected to said second controlled valve open and the other second controlled valve(s) being closed, a third controlled valve mounted at the outlet of said buffer tank being closed, and a step of emptying said buffer tank, said second controlled valve being closed and said third controlled valve being open,the gas flowing through a regulator mounted at the outlet of said third controlled valve to supply said water, less one consumer organ. The use of on / off valves makes it possible to control the quantity of liquid passing through the valve by the duration of opening.

[0022] In one embodiment, in normal operation, a first buffer tank is being filled with liquid by pressure balancing by one of at least one first valve open and the second valve corresponding to said first buffer tank open, the third valve corresponding to said first buffer tank being closed, while a second buffer tank is being supplied with pressurized gas, the second valve corresponding to said second buffer tank closed, the third valve corresponding to said first buffer tank being open. This mode is suitable for two buffer tanks.

[0023] In one embodiment, a third buffer tank is being gasified, the second valve corresponding to said third buffer tank being closed, the third valve corresponding to said third buffer tank being closed. This mode is suitable for three or more buffer tanks.

[0024] In one embodiment, the step of emptying said buffer tank comprises a sub-step of emptying by a pressure reducer to reduce the gas pressure to the pressure requested by the consumer member, then a sub-step of emptying assisted by a pump to bring the gas pressure to the pressure requested by the consumer member and bring the pressure in said buffer tank at the end of the emptying to a value lower than the pressure existing in the cryogenic distributor. A more complete emptying of the buffer tank is obtained.

[0025] In one embodiment, the capacity of the buffer tanks is calculated to ensure flight autonomy for the aircraft according to the standards in force in the event of an incident affecting the energy reserve, in particular on a buffer tank if two buffer tanks are present, and on two buffer tanks if three buffer tanks are present.

[0026] Other characteristics and advantages of the invention will appear on examining the detailed description below, and the appended drawings, in which:

[0027] [Fig.1] schematically illustrates a device according to one aspect of the invention with two cryogenic tanks and three buffer tanks.

[0028] [Fig.2] schematically illustrates a device according to one aspect of the invention with a cryogenic tank and three buffer tanks.

[0029] [Fig. 3] schematically illustrates a device according to one aspect of the invention with a cryogenic tank and three buffer tanks.

[0030] [Fig. 4] schematically illustrates a device according to one aspect of the invention with two cryogenic tanks and three buffer tanks.

[0031] [Fig.5] schematically illustrates a device according to one aspect of the invention with a cryogenic tank and two buffer tanks.

[0032] The attached drawings may not only serve to complete the invention, but also contribute to its definition, where appropriate.

[0033] The aeronautical gas distribution device is designed to be carried by an aircraft: airplane, drone, helicopter, etc. The aeronautical gas distribution device is supplied with liquid and provides gas under a chosen pressure. In other words, the fuel or oxidizer is stored at very low temperature in liquid form in a cryogenic tank. As an embodiment, gaseous hydrogen at 0°C and 1 atmosphere has a density approximately 800 times lower than liquid hydrogen at -253°C, therefore a volume approximately 800 times higher. A cryogenic tank is unable to withstand high pressures, particularly those above 10 bars.

[0034] The stored gas is chosen from hydrogen, methane, ethane, ethylene, acetylene and oxygen.

[0035] Furthermore, aeronautical maintenance regulations require that most aircraft parts be dismantled and repaired or replaced. Thus, an aircraft is capable of landing anywhere - an aerodrome for an airplane, a landing pad for a helicopter - suitable for its weight and landing requirements but not equipped with maintenance equipment specific to the aircraft model. In the event of detected damage, the aircraft is configured to be repaired, permanently or temporarily, or dismantled in order to replace or repair a defective component, in accordance with the manufacturer's manuals and documents approved by the aviation safety authorities. It is desirable that the component be easily accessible to a maintenance operator. In the event of replacement, it is desirable that the component be as small as possible. for easy handling and transport. In the event of repair, it is desirable that the component be repairable using proven and common tools and processes in the aeronautical field.

[0036] An aircraft is subject to daily, weekly, etc. inspection visits, immobilizing the aircraft for a duration inverse to the frequency.

[0037] The aeronautical gas distribution system is therefore subject to such requirements.

[0038] The Applicant has identified a need for gas distribution from aeronautical cryogenic tanks whether structurally linked to the structure of the aircraft, installed in the aircraft or carried by the aircraft.

[0039] From another perspective, aircraft are currently subject to a maximum distance rule from a runway expressed in flight hours according to ETOPS certification. This distance depends on the type of aircraft.

[0040] Wishing to ensure a high level of safety as well as a perception of this safety by users, the Applicant identified the need to fly even in the event of damage to the cryogenic tank requiring release into the atmosphere of the contained gas.

[0041] The aeronautical storage device aims to satisfy the complex need thus analyzed by the Applicant.

[0042] As illustrated in Figure 1, the aeronautical gas distribution device 1 on board an aircraft is supplied by sources of liquefied gas2 to supply gas to one or more consumer members 3. Here, two consumer members 3 have been shown, for example two thrusters, an electric power generator or an air heater. A flow meter 22 is arranged at the outlet of each source of liquefied gas2.

[0043] Liquefied gas sources2 consist of two cryogenic tanks arranged in parallel. Each cryogenic tank is equipped with an outlet pipe 4. The terms upstream and downstream refer to the direction of flow of the fluid, liquid then gas, during normal operation.

[0044] Each cryogenic tank is insulated to contain liquefied gas, for example liquid hydrogen at -253°C. Each cryogenic tank is capable of withstanding a maximum working pressure of around 6 to 10 bars.

[0045] The aeronautical gas distribution device 1 comprises a first valve 11 for each cryogenic tank. The first valve 11 is mounted on the outlet pipe 4. The first valves 11 are controlled with an open position and a closed position. The intermediate positions of the first valves 11 are dynamic in the sense that the first valves 11 are in motion while passing into said intermediate positions. In other words, the first valves 11 are on / off. The first valves 11 may be arranged immediately downstream of the flow meters 22. Optionally, the flow meters 22 are downstream of the first valves 11.

[0046] The first valves 11 open into a cryogenic distributor 5. The cryogenic distributor 5 may comprise a common pipe 6 connecting the outlets of the first valves 11. The distributor is cryogenic in the sense that it sees liquefied gas pass through it.

[0047] The cryogenic distributor 5 comprises a plurality of outlets, here three. On each of said outlets are mounted second valves 12. The second valves 12 are controlled with an open position and a closed position. The intermediate positions of the second valves 12 are dynamic in the sense that the second valves 12 are in motion while passing into said intermediate positions. In other words, the second valves 12 are all or nothing. The second valves 12 are here three in number.

[0048] Downstream of each second valve 12 is mounted a buffer tank 7. Three buffer tanks 7 are provided in this embodiment. Each buffer tank 7 also serves as a gasifier. Insulation can be avoided. Each buffer tank 7 receives liquid and supplies gas downstream. A pressure increase or gasification step occurs in each buffer tank 7 between filling and emptying. Each buffer tank 7 is capable of withstanding a maximum operating pressure of the order of 300 to 1000 bar. Each buffer tank 7 is designed to operate in a temperature range of -253 °C to +60 °C. The buffer tanks 7 are two-phase on a part of the operating stages and single-phase gases on the other operating stages. Each buffer tank 7 can be equipped with a heating member 8.

[0049] Downstream of each buffer tank 7 is installed a third valve 13 to supply gas and a pressure reducer 9 downstream of the third valve 13. The pressure reducer 9 limits the pressure to supply gas at a consumption pressure set by the manufacturer of the consumer member 3. The pressure reducer 9 is active when the pressure in the buffer tank 7 is higher than the consumption pressure and inactive otherwise. The consumption pressure is lower than the maximum pressure of the buffer tank 7. The consumption pressure is independent of the maximum pressure of the cryogenic tanks. The third valves 13 are on / off.

[0050] Downstream of each regulator 9, a fourth controlled valve 14 can be provided. The fourth valves 14 are all or nothing.

[0051] The fourth valves 14 or the regulators 9, depending on the option chosen, open into a manifold 10. The manifold 10 may comprise a pipe connecting the outlets of the fourth valves 14 or the regulators 9. The manifold 10 sees gas pass through. The manifold 10 is connected downstream to supply pipes 23 to the consumer members 3. In general, a supply pipe 23 is provided for each consumer member 3. Each supply pipe 23 may be equipped with a controlled supply valve 24. The supply valve 24 has a variable flow rate.

[0052] The aeronautical gas distribution device 1 comprises at least one compressor 20 connected to the manifold 10. In general, two compressors 20 are provided in parallel for redundancy. The compressor 20 is electric. The compressor 20 may be equipped with a controlled upstream valve. The compressor 20 delivers gas into the manifold 10. In particular, the manifold 10 consists of a pipe in the case of a single consumer member 3.

[0053] Downstream of each buffer tank 7 is installed a fifth valve 15 to supply gas and a second manifold downstream of the fifth valves 15. The second manifold is connected to the compressor 20. The fifth valves 15 allow the buffer tanks 7 and the compressor 20 to be isolated. The fifth valves 15 are controlled. The fifth valves 15 are all or nothing.

[0054] The compressor 20 increases the pressure to supply gas at a pressure equal to a consumption pressure set by the manufacturer of the consumer member 3. The consumption pressure is lower than the maximum pressure in the buffer tank 7. The compressor 20 makes it possible to take gas from a buffer tank 7 whose pressure is lower than the consumption pressure to supply the collector 10 and the consumer members 3. A more complete emptying of the buffer tank 7 makes it possible to increase the autonomy provided by the gas contained in a buffer tank 7 or to reduce the volume of the buffer tank 7.

[0055] Emptying the buffer tank 7 sufficient to bring the internal pressure of the buffer tank 7 to a value lower than the pressure in one of the cryogenic tanks allows, during filling following emptying, the transfer of the liquid from the cryogenic tank to the buffer tank 7 by pressure difference. Thus, the liquid from the cryogenic tank is sucked by the buffer tank 7 until pressure equilibrium is reached. A cryogenic pump can be dispensed with, resulting in a saving in mass and energy consumption.

[0056] The aeronautical gas distribution device 1 offers a combination of individual states of each cryogenic tank, each buffer tank 7 and each consumer member 3. Several consumer members 3 can be active simultaneously. In normal mode, one cryogenic tank is being emptied while the others are inactive and therefore closed. However, in certain situations, for example to reduce the pressure in several cryogenic tanks, a particular mode can be provided in which several cryogenic tanks are being emptied. The buffer tanks 7 have a filling mode, a gasification mode, a gas storage mode and an emptying mode.

[0057] When one of the cryogenic tanks is being emptied, the corresponding first valve 11 is open and the other first valves 11 are closed. When one of the consumer members 3 is being supplied, the corresponding supply valve 24 is open.

[0058] When one of the buffer tanks 7 is in filling mode, the second valve 12 connected to said buffer tank 7 is open and at least one of the first valves 11 is open. The other second valves 12 are closed except in the case where simultaneous filling of two buffer tanks 7 is carried out. The third valve 13 connected to said buffer tank 7 is closed. The fifth valve connected to said buffer tank 7 is closed.

[0059] When one of the buffer tanks 7 is in gasification mode, the second valve 12 connected to said buffer tank 7, the third valve 13 connected to said buffer tank 7 and the fifth valve 15 connected to said buffer tank 7 are closed. The gasification mode is of short duration, in particular in the case of a warm ambient atmosphere and / or heating of the buffer tank 7.

[0060] When one of the buffer tanks 7 is in draining mode, the second valve 12 connected to said buffer tank 7 is closed. In the first part of draining, the pressure in the buffer tank 7 is higher than the consumption pressure. The third valve 13 connected to said buffer tank 7 is open, the corresponding fourth valve 14 is open and the fifth valve connected to said buffer tank 7 is closed. The gas undergoes a pressure reduction in the pressure reducer 9 and is supplied to the manifold 10 at the consumption pressure. The gas is then consumed by the consumer member(s) 3.

[0061] At any given time, among three buffer tanks 7, one is in filling mode, another in gasification then storage mode and the third in emptying mode. Since the modes have different durations, we can also find two buffer tanks 7 in filling mode and the third in emptying mode or vice versa. We can also find two buffer tanks 7 in storage mode and the third in emptying mode or vice versa.

[0062] In the embodiment, a flow meter 22 is arranged at the outlet of each source of liquefied gas 2. The flow meters 22 make it possible to know with sufficient precision the quantity of liquid supplied to such buffer tank 7.

[0063] In the embodiment, the aeronautical gas distribution device 1 comprises a control unit 25 receiving an external instruction, for example from the consumer organs 3 or from a central control unit of the aircraft, and liquid flow rate data from the flow meters 22. The control unit 25 generates and sends setpoints to said first, second, third, fourth and fifth controlled valves and to the controlled supply valves 24. The setpoints can be "open" or "closed". The control unit 25 manages said combination of individual states.

[0064] Alternatively, the first valves 11 may be replaced by at least one multi-way valve having several inlets and one outlet. In this case, it is advantageous to provide a multi-way valve with mixed positions, in particular at least one position for simultaneously draining two or more sources of liquefied gas 2 to reduce the pressure while avoiding loss into the atmosphere.

[0065] Alternatively, the second valves 12 can be replaced by at least one multi-way valve having an inlet and several outlets, one per buffer tank 7. Said multi-way valve forms a distributor.

[0066] Alternatively, the regulators 9 are replaced by a single regulator 9, the third valves 13 opening into the single regulator 9. In this case, the third valves 13 can be replaced by at least one multi-way valve having several inlets and one outlet to the regulator. The fourth valves 14 are then replaced by a single fourth valve 14, possibly not piloted.

[0067] Alternatively, the fifth valves 15 can be replaced by at least one multi-way valve having several inlets, one per buffer tank 7, and an outlet to the compressor 20 or compressors 20. Said multi-way valve forms a manifold 10.

[0068] In the embodiment shown in Figure 2, the device is associated with a source of liquefied gas 2 to fill three buffer tanks 7 supplying two gas consuming members 3. The first valves 11 can be omitted in the sense that the second valves 12 are sufficient to direct the flow of liquid from the source of liquefied gas 2 to one of the buffer tanks 7.

[0069] Furthermore, the regulator 9 is unique. The fourth valve 14 is unique. The regulator 9 is connected downstream of the third valves 13, here three in number, to receive pressurized gas from the buffer tank 7, the associated third valve 13 of which is open. This is also suitable for the case of Figure 5 with two buffer tanks 7 instead of three. The single regulator 9 is also suitable for the other embodiments shown regardless of the number of liquefied gas sources 2 and the number of consumer units 3.

[0070] The flow meters 22 are arranged between the second valves 12 and the buffer tanks 7. Optionally, the flow meters 22 are arranged upstream of the second valves 12.

[0071] The compressors 20 are controlled remotely wirelessly by the control unit 25.

[0072] In the embodiment shown in Figure 3, the device is associated with a source of liquefied gas 2 to fill three buffer tanks 7 supplying a gas consuming member 3, for example a propellant. The first valve 11 can be omitted for the same reasons as for Figure 2. The flow meter 22 is arranged at the outlet of the source of liquefied gas 2. The presence of three buffer tanks 7 ensures significant autonomy for the aircraft in the event of a fault in the source of liquefied gas 2, a fault which may require emptying of the source of liquefied gas 2. In addition, three buffer tanks 7 provide redundancy in the sense that the device can operate satisfactorily with only two buffer tanks 7. The cryogenic distributor 5 can comprise a valve with one inlet and three outlets, one per buffer tank 7.The supply valve 24 associated with the consumer member 3 can be omitted, in particular if the valves associated with the compressors 20 are controlled.

[0073] This embodiment is well suited to aircraft provided with two assemblies each comprising an aeronautical gas distribution device 1 and at least one cryogenic source of liquefied gas. Each assembly can be mounted symmetrically in the aircraft, for example in the wings, under the wings, etc.

[0074] In the embodiment shown in Figure 4, the device is associated with two sources of liquefied gas 2 to fill three buffer tanks 7 supplying a gas consuming member 3.

[0075] In the embodiment shown in Figure 5, the device is associated with a source of liquefied gas 2 to fill two buffer tanks 7 supplying a gas consuming member 3. The first valve 11 can be omitted for the same reasons as for Figure 2. The operation is then adapted. The duration of the gasification phase can be reduced, in particular by a heating member 8 for each buffer tank 7 or for the buffer tanks 7. Furthermore, one of the buffer tanks 7 empties through the third valve 13 then through the fifth valve 15 while the other of the buffer tanks 7 fills with liquid and is then in the gasification phase. The switching time between the third valve 13 and the fifth valve 15 is independent of the closing time of the second valve 12.

[0076] Generally, the number X of cryogenic tanks, the number Y of buffer tanks 7 and the number Z of consumers are independent, with X>1; Y>2; Z>1.

[0077] The volume capacity of each buffer tank 7 is between 10 and 20% of the volume capacity of each liquefied gas source 2.

[0078] Since the cryogenic tanks 2 are subject to evaporation of liquefied gas, a gas collection circuit may be provided in an upper portion of the cryogenic tanks 2. The collection circuit may be activated above a threshold pressure by a calibrated pressure valve. The collection circuit comprises a compressor for reinjecting the gas downstream, for example between the fifth valves 15 and the compressor 20.

[0079] Optionally, additional flow meters are placed at the inlet of each buffer tank. Redundancy of liquid flow measurement is ensured.

[0080] The first valves 11 may be monostable or bistable. The first valves 11 may be controlled to open for a duration corresponding to a filling of one of the buffer tanks 7, or by pulse width modulation. The second valves 12 may be monostable or bistable. The second valves 12 may be controlled to open for a duration corresponding to a filling of one of the buffer tanks 7, or by pulse width modulation, i

Claims

Demands

1. An aeronautical gas distribution device (1) in an aircraft between at least one liquefied gas source (2) and at least one gas-consuming component (3), comprising at least one first on / off valve (11) controlled at the outlet of each liquefied gas source (2), a cryogenic distributor (5) connected to each first controlled valve (11) and supplied with liquid, second on / off controlled valves (12) connected in parallel to the cryogenic distributor (5), two-phase buffer tanks (7) supplied with liquid, each by one of said second controlled valves (12), and supplying gas, third controlled valves (13) mounted at the outlet of each buffer tank (7) to supply gas, a regulator (9) mounted at the outlet of the third controlled valves (13), a manifold (10) supplied by the regulator (9) to supply said at least one consumer organ (3).

2. Device according to claim 1, comprising fourth controlled valves (14) mounted at the outlet of each regulator (9), for supplying gas.

3. Device according to any one of the preceding claims, comprising at least one compressor (20) supplied by at least one of the buffer tanks (7), and at least one fifth controlled valve (15) mounted between the compressor (20) and said buffer tank (7).

4. Device according to any one of the preceding claims, comprising a control unit controlling at least a first valve (1 1 ) controlled for sequential filling of the buffer tanks (7) by pressure difference and sequential emptying of the buffer tanks (7).

5. A device according to claim 3 or 4, wherein, for emptying one of the buffer tanks (7), the control unit operates the third valves, initially controlled for gas flow by pressure differential, and subsequently by actuation of a compressor (20) in a second step until a pressure is obtained in said buffer tank (7) lower than the pressure existing in the cryogenic distributor (5).

6. Device according to any one of the preceding claims, wherein at least one first valve (11) and the second valves (12) are cryogenic and wherein a flowmeter (22) is disposed at the outlet of each liquefied gas source (2), additional flowmeters being advantageously disposed at the inlet of the buffer tanks (7).

7. Assembly comprising a device according to any one of the preceding claims, and at least one single cryogenic source of liquefied gas.

8. An aeronautical method for distributing gas in an aircraft between at least one liquefied gas source (2) and at least one gas-consuming component (3), comprising a step of filling a buffer tank (7) from among at least two buffer tanks (7) with liquefied gas, by at least one from among at least one first valve (11), on / off, controlled at the outlet of each liquefied gas source (2), a cryogenic distributor (5) connected to each first controlled valve (11), supplied with liquid by the cryogenic distributor (5), one from among second on / off controlled valves (12) connected to the cryogenic distributor (5) in parallel, said buffer tank (7) being connected to said second controlled valve (12) open and the other second controlled valve(s) (12) being closed, a third controlled valve (13) mounted at the outlet of said buffer tank (7) being closed, and a step of emptying said buffer tank (7),said second controlled valve (12) being closed and said third controlled valve (13) being open, the gas flowing through a regulator (9) mounted at the outlet of said third controlled valve (13) to supply said at least one consuming device (3).

9. The method according to claim 8, wherein, in normal operation, a first buffer tank (7) is being filled with liquid by pressure equalization through at least one of the first valves (11) being open and the corresponding second valve (12) first buffer tank (7) open, the third valve (13) corresponding to said first buffer tank (7) being closed, while a second buffer tank (7) is being supplied with pressurized gas, the second valve (12) corresponding to said second buffer tank (7) closed, the third valve (13) corresponding to said first buffer tank (7) being open, and a third buffer tank (7) is being gasified, the second valve (12) corresponding to said third buffer tank (7) being closed, the third valve (13) corresponding to said third buffer tank (7) being closed.

10. A method according to claim 8 or 9, wherein the emptying step of said buffer tank (7) comprises a substep of emptying by a pressure regulator (9) to reduce the gas pressure to the pressure required by the consuming member (3), then a substep of emptying assisted by a pump to bring the gas pressure to the pressure required by the consuming member (3) and to bring the pressure in said buffer tank (7) at the end of the emptying to a value lower than the pressure existing in the cryogenic distributor (5).