A direct fueling station and a method of refueling are provided. The station includes an insulated tank for storing a liquefied fuel, a pump, at least a heat exchanger, a control unit, a dispenser including a flow meter, a flow control device, and at least one sensor for testing pressure and/or temperature. The heat exchanger converts liquefied fuel from pump into a gaseous fuel, which is added into an onboard fuel tank in a vehicle. The control unit includes one or more programs used to coordinate with the pump, the flow meter, the flow control device, and/or the sensor(s) so as to control a refueling method. A peak electrical power requirement is less than that determined by the product of a rated volumetric flow rate of the pump and a rated pumping pressure adequate for a fill pressure of the vehicle. A computer implemented system having the program(s) is also provided.

An apparatus includes a high-pressure tank, a controller, a valve, controlled by the controller, and a compressor.

A power supply 100 is described. The power supply 100 has a first electrical outlet 110 and comprises: optionally a set of hydrogen storage devices 200, including a first hydrogen storage device 200A, a set of heaters 300, including a first heater 300A, a first releasable fluid inlet coupling 410 and/or a first releasable fluid outlet coupling 510; wherein the first hydrogen storage device 200A comprises: a pressure vessel 230A, having a first fluid inlet 210A and a first fluid outlet 220A, comprising therein a thermally conducting network 240A optionally thermally coupled to the first heater 300A, wherein the pressure vessel 230A is arranged to receive therein a hydrogen storage material 250A in thermal contact, at least in part, with the thermally conducting network 240A, wherein the first fluid inlet 210A and/or the first fluid outlet 220A are in fluid communication with the first releasable fluid inlet coupling 410 and/or the first releasable fluid outlet coupling 510, respectively; and preferably, wherein the thermally conducting network 240A has lattice geometry and/or a fractal geometry in two and/or three dimensions.

Some embodiments are directed to a module for depressurisation and storage of a portion of a gas layer coming from at least one cryogenic tank. Some other embodiments are directed to a system using such a module.

A system for dispensing cryogenic liquid includes a container defining an interior with a partition dividing the interior into primary and reserve chambers. Cryogenic liquid within the primary chamber is separated from cryogenic liquid in the reserve chamber. The partition provides a headspace cornrnurrrcation passage. A primary pressure building circuit has an inlet selectively in liquid communication with the primary chamber and an outlet in fluid communication with the headspaces of the primary and reserve chambers. A reserve pressure building circuit has an inlet selectively in liquid communication with the reserve chamber and an outlet in fluid communication with the headspaces of the primary and reserve chambers. An equalizing circuit is selectively in liquid communication with the primary and reserve chambers. A dispensing line is selectively in liquid communication with the primary chamber.

Process for vaporizing purge liquid from a cryogenic liquid vaporizer, the liquid containing at least one impurity, in which the purge liquid is withdrawn from a bath of liquid surrounding the vaporizer or resulting from the vaporizer, all of the purge liquid is vaporized in a heater, characterized in that the content of the at least one impurity in at least one portion, or even all of the heated vaporized liquid is analysed and the flow rate of at least one portion, or even all of the heated vaporized liquid is measured.

A station and method for refilling a tank or tanks with pressurized gas in which liquefied gas is vaporized in a vaporizer. One portion of the vaporized gas is compressed to produce a compressed gas. Another portion of the vaporized gas is not compressed but instead is fed to a heat exchanger where it is used to cool the compressed gas. The thus-warmed gas is reinjected into a filling line that feeds the liquefied gas to the vaporizer.

A fluid transfer apparatus transfers fluid from a first bulk storage vessel at a gas pressure equal to or greater than a first gas pressure. The fluid transfers to a first or second supply vessel; each having a gas pressure equal to or less than a second pressure. The second pressure less than the first pressure. The fluid transfer continues until the fluid in the first or second supply vessel reaches a predetermined weight inside the first or second supply vessel. The fluid in the filled first or second supply vessel, at the predetermined weight, under a pressure equal to or less than the second pressure; and the fluid in a liquefied and gas state. The apparatus heats the fluid in the first or second supply vessel, filled to the predetermined weight, to bring the fluid in the first or second supply vessel to a third gas pressure. The third gas pressure higher than the first gas pressure and the second gas pressure. The fluid in the first or second supply vessel having the third gas pressure can include fluid in the liquefied gas state and gas state or super critical state.

Pressurized gas tanks are filled from at least one gas source using a transfer circuit, a set of buffer storage tanks and at least one compressor. The set of buffer storage tanks may be filled with pressurized gas from the at least one gas source by pressure balancing via balancing lines without going through the at least one compressor. The set of buffer storage tanks may also be filled with pressurized gas from the at least one gas source that is compressed by the at least one compressor.

A gas supply system 100 comprises: a first vaporization supply device 10A including a first vaporization section 12A having a heater, a first valve 14A, and a first supply pressure sensor 16A for measuring a gas pressure between the first vaporization section and the first valve; a second vaporization supply device 10B including a second vaporization section 12B having a heater, a second valve 14B, and a second supply pressure sensor 16B for measuring a gas pressure between the second vaporization section and the second valve; and a control circuit 20. The system is configured to flow a gas from the first vaporization section 10A and a gas from the second vaporization section 10B sequentially into a common flow path, by shifting timings of an opening period of the first valve 14A and an opening period of the second valve 14B.