A method for liquid air and gas energy storage (LAGES) which integrates the processes of liquid air energy storage (LAES) and regasification of liquefied natural gas (LNG) at the import terminal through the exchange of thermal energy between the streams of air and natural gas (NG) in their gaseous and liquid states and includes harnessing the LNG as an intermediate heat carrier between the air streams being regasified and liquefied, recovering a compression heat from air liquefier for LNG regasification and utilizing a cold thermal energy of liquid air being regasified for reliquefaction of a part of send-out NG stream with its return to LNG terminal.

A compressed gas energy storage system may include an accumulator for containing a layer of compressed gas atop a layer of liquid. A gas conduit may have an upper end in communication with a gas compressor/expander subsystem and a lower end in communication with accumulator interior for conveying compressed gas into the compressed gas layer of the accumulator when in use. A shaft may have an interior for containing a quantity of a liquid and may be fluidly connectable to a liquid source/sink via a liquid supply conduit. A partition may cover may separate the accumulator interior from the shaft interior. An internal accumulator force may act on the inner surface of the partition and the liquid within the shaft may exert an external counter force on the outer surface of the partition, whereby a net force acting on the partition is less than the accumulator force.

A storage system for temporary storage of a gas comprising a storage vessel configured to store a pressurized gas or liquid; at least one of a compressor configured to pressurize the gas and provide the pressurized fluid or a liquefaction apparatus operable to liquefy the gas to provide the liquid; and piping associated with one or more valves, wherein the piping and the associated one or more valves are configured to provide: (a) in a first configuration, inflow of the gas into the compressor or the liquefaction apparatus, wherein the compressor is configured to pressurize the inflowing gas to provide the pressurized fluid or wherein the liquefaction apparatus is configured to liquefy the inflowing gas to provide the liquid, and introduce the pressurized gas or the liquid into the temporary storage vessel; and (b) in a second configuration, outflow of the pressurized gas or liquid from the temporary storage vessel.

A thermal storage subsystem may include at least a first storage reservoir disposed at least partially under ground configured to contain a thermal storage liquid at a storage pressure that is greater than atmospheric pressure. A liquid passage may have an inlet connectable to a thermal storage liquid source and configured to convey the thermal storage liquid to the liquid reservoir. A first heat exchanger may be provided in the liquid inlet passage and may be in fluid communication between the first compression stage and the accumulator, whereby thermal energy can be transferred from a compressed gas stream exiting a gas compressor/expander subsystem to the thermal storage liquid.

A power plant for energy production from a liquid gas product stored in a cryogenic storage tank, and comprises a container housing and an inlet to receive the gas product from the tank via a line. An evaporation unit converts the liquid gas product to a gaseous phase. The plant comprises an aggregate for the combustion of the gaseous phase to provide an electrical current to an external consumer. A circuit brings the liquid and/or gaseous phase to the motor via the evaporation unit. A regulating unit regulates the pressure and/or temperature. The liquid gas product is supplied to the motor in the gaseous phase by passive liquid and gas transport. A cooling circuit transfers heat from the motor to a heat exchanger in the evaporation unit.

A system for better utilization of liquefied natural gas (LNG) on gasification of the liquid includes a gas power generation subsystem, a steam power generation subsystem, an energy storage subsystem, and a cooling subsystem. A gasification device of the gas power generation subsystem renders the LNG gaseous and collects cold energy generated during the gasification. The gas is supplied to the gas power generation device for generating electrical power and the cold energy is supplied to the steam power generation subsystem and the cold storage subsystem. Electrical power generated by the gas power generation subsystem and the steam power generation subsystem is supplied to the cooling subsystem, and the energy stored in the energy storage subsystem is also supplied to the cooling subsystem.

Disclosed is a paired compress gas energy power system and power method. The paired compress gas energy power system includes: a paired compress gas energy storage device having a high pressure air container and a low pressure air container, the high pressure air container is filled with a high pressure gas, the low pressure air container is filled with a low pressure gas; a paired compress gas energy engine, respectively connected to the low pressure air container and the high pressure air container; and a power device connected to the rotary shaft of the paired compress gas energy engine, the power device is driven by the paired compress gas energy engine. The invention converts the paired compress gas energy into the mechanical torque energy through the paired compress gas energy engine to drive the power device to work, or to drive the generator to generate electric energy.

A method for liquid air and gas energy storage (LAGES) which integrates the processes of liquid air energy storage (LAES) and regasification of liquefied natural gas (LNG) at the Floating Storage, Regasification and Power (FSRP) facilities through the exchange of thermal energy between the streams of air and natural gas (NG) in their gaseous and liquid states and includes recovering a compression heat from air liquefier and low-grade waste heat of power train for LNG regasification with use of an intermediate heat carrier between the air and LNG streams and utilizing a cold thermal energy of liquid air being regasified for increase in LAGES operation efficiency through using a semi-closed CO.sub.2 bottoming cycle.

A hydrogen refueling system including a hydrogen center enclosure fluidly connected to a dispenser by a supply pipe, a first portion of the supply pipe disposed within the hydrogen center enclosure and a second portion of the supply pipe extending between the hydrogen center enclosure and the dispenser, a cooling system having a first cooling circuit for cooling the supply pipe and a second cooling circuit for cooling the second portion of the supply pipe, and a controller, where the second cooling circuit has a return path fluidly connected to a forward path, where the second cooling circuit is thermally connected to the second portion of the supply pipe, and the controller initiates cooling of the supply line by the forward path or return path of the second cooling circuit when the temperature of the supply line is higher than a threshold value.

A system for filling an LPG vehicle with LPG using an auxiliary bombe is provided. The system may be configured for easily filling a main bombe with LPG even in the hot season (summertime) or the like during which the outside temperature rapidly rises, by using an auxiliary bombe in addition to using the main bombe. The system may also be capable of always smoothly refilling the main bombe with LPG by moving a portion of the LPG in the main bombe to the auxiliary bombe, when the pressure in the main bombe is higher than the LPG filling pressure of a filling gun in the hot season during which the outside temperature rapidly rises, so that the pressure in the main bombe becomes lower than the filling pressure.