The invention relates to a compressed air energy storage system comprising a pressure accumulator (2) for gas to be stored under pressure, and a heat accumulator (27) for storing the compression heat that has accumulated during charging of the pressure accumulator (2), wherein the heat accumulator (27) is arranged ready for use in an overpressure zone (31). Said arrangement enables a structurally simple heat accumulator to be provided, since said heat accumulator is not loaded by the pressure of the gas passing therethrough.

A method for supplying gas to a gas-consuming apparatus provided on a ship including a tank containing the gas in the liquid state and in the gaseous state, in which the method includes: supplying the gas-consuming apparatus with gas withdrawn in the gaseous state from the tank and by a supply unit; condensing at least a part of the gas withdrawn in the gaseous state from the tank by a condensation unit having at least one heat exchanger configured to perform a heat exchange between gas withdrawn between the supply unit and the gas-consuming apparatus and gas flowing between the tank and the supply unit; and cooling the heat exchanger prior to the condensing and at least partially simultaneously with the supplying.

A system for cooling compressed natural gas comprises a compressed natural gas coil located within a compartment. The compressed natural gas coil has a compressed natural gas inlet and a compressed natural gas outlet. The system also comprises a refrigerant coil located within the compartment. The refrigerant coil has a refrigerant inlet and a refrigerant outlet. The system further comprises a heat transfer fluid located within the compartment. The heat transfer fluid thermally connecting the compressed natural gas coil to the refrigerant coil.

Plant and method for storing and distributing pressurized liquefied cryogenic fluid, comprising a liquefied gas source and a distribution member, comprising a first fluid inlet connected to the liquefied gas source and a second end intended to be connected to a user of the pressurized liquefied gas supplied by the distribution member, the source comprising a first liquefied gas store configured to store and supply the liquefied gas to the distribution member at a first determined pressure, the source comprising a second liquefied gas store configured to store the liquefied gas at a second determined pressure which is lower than the first pressure, the plant comprising a connecting pipe having a valve assembly connecting the first and second liquefied gas stores, the plant comprising a filling pipe having a valve assembly and having a first end connected to the second liquefied gas store and a second end intended to be connected to a mobile store for supplying liquefied gas to fill the source.

Method for filling a tank with pressurized hydrogen via a filling station comprising at least one buffer container and a fluid circuit connected to said at least one buffer container, the circuit of the filling station comprising a first end connected to at least one source of hydrogen gas, the circuit comprising a second end fitted with a transfer pipe intended to be connected removably to the tank that is to be filled, the method involving a step of cooling the hydrogen supplied to the tank by transferring negative calories between a cold source and the hydrogen, the method being characterized in that it comprises a step of purifying the hydrogen supplied by the source in a purification member before transferring it to the at least one buffer container, and in that it comprises a step of transferring negative calories from said cold source to the hydrogen before and/or during the purification step.

A power-saving type liquefied-gas-fuel ship includes: a liquefied gas storage tank storing liquefied gas; an engine using the liquefied gas stored in the liquefied gas storage tank or boil-off gas generated by spontaneous vaporization of the liquefied gas as fuel; a fuel feeder supplying the liquefied gas as fuel for the engine; a compressor compressing the boil-off gas to a pressure required for the engine; a heat exchanger cooling the remaining boil-off gas not supplied to the engine among the boil-off gas compressed by the compressor; a refrigerant circulation line in which the refrigerant supplied to the heat exchanger circulates; a refrigerant compressor compressing the refrigerant discharged from the heat exchanger after heat exchange in the heat exchanger; and a cold heat recovery device recovering cold heat of the liquefied gas supplied as fuel for the engine to cool the refrigerant compressed by the refrigerant compressor.

Systems and techniques that facilitate scalable thermal energy recycling for cryogenic systems are provided. In various embodiments, a system can comprise at least one cryostat. In various aspects, the system can further comprise a thermal battery coupled to the at least one cryostat by a thermal exchange system. In various instances, the thermal battery can be configured to store thermal energy extracted from the at least one cryostat or to supply thermal energy to the at least one cryostat.

The invention provides an apparatus comprising a storage tank, a liquid piston compressor and a gas-fed device. The storage tank is configured to store liquefied gas therein. The liquid piston compressor is disposed downstream of, and in fluid communication with, the storage tank and is configured to receive boil-off gas from the storage tank and to compress the gas. The gas-fed device is disposed downstream of, and in fluid communication with, the liquid piston compressor, and is configured to receive compressed gas from the liquid piston compressor.

Provided are a thermoelectric power generation module, a thermoelectric power generation apparatus including the same, an anti-icing vaporization device including the same, and an apparatus for a vaporized fuel gas liquefaction process including the same. The thermoelectric power generation module includes: a pipe through which a fluid flows; and a thermoelectric power generator configured to surround the pipe and to produce power due to a temperature difference between the fluid and outside air.

Method and apparatus for reliquefying and returning boil-off gas (BOG) to a liquefied natural gas (LNG) tank, the method including: Withdrawing BOG (F2) from the headspace of an LNG tank; compressing the BOG in a first compression stage to a first pressure p.sub.1 between 8 and 18 bara and tapping of a first portion of this gas; further compressing a second portion of the gas from step in a final compression stage to a second pressure p.sub.2?120 bara; cooling at least part of the further compressed gas to a first temperature T.sub.1 between ?20? C. and ?100? C.; expanding the gas from step to a third pressure p.sub.3 between 8 and 20 bara; and separating the gas from step into a liquid phase and a gaseous phase to combine the gaseous phase with the tapped first portion of the gas from the first compression stage and to return the liquid phase into the LNG tank.