A vaporizer system includes a defrosting function along with the ability to convert liquefied gas to a use gas. The vaporizer system includes first and second vaporizers and piping that transfers fluid from an inlet port to an outlet port with a portion of the piping being between the first and second vaporizer. The system also includes a trim heater and a number of valves for regulating flow of the fluid through the transfer piping. The valves may be placed in a first configuration where vapor from the first vaporizer is heated and directed to the second vaporizer so that the second vaporizer is defrosted and a second configuration where vapor from the second vaporizer is heated and directed to the first vaporizer so that the first vaporizer is defrosted.

A System to convert and dispense pressurized gas(es) of cryogenic liquids of gas(es), and systems and methods using a sphere pressure vessel to efficiently convert liquid natural gas (LNG) to compressed natural gas (CNG) and low pressure natural gas (NG) and other cryogenic liquids of gas. The system requires one dedicated sphere pressure vessel at the dispensing location and the location of elements according to horizontal and vertical orientation to convert, retain, store, and dispense multiple pressures of gas from a cryogenic liquid supply such as a non-dedicated high pressure cryogenic personal supply tank. The system efficiently modifies and controls parameters of volume, pressure, and temperature in conversion scale to retain all converted product under human control to dispense, without process required waste, for use in commercial, utility and industrial uses, and scaleable for single family residential applications where service can be accomplished by pickup truck and trailer, where semi trucks access is not available.

A gas supply system includes a first tank, a first path into which a first gas generated by vaporization of a first low-temperature liquefied gas flows, a gas boosting mechanism being disposed in the first path, a second path that is a path configured to extract the first low-temperature liquefied gas from the first tank, a pump and a vaporization mechanism being disposed in the second path and a reliquefaction path that is a path configured to liquefy at least part of the first gas extracted from an upstream side of the gas boosting mechanism in the first path and to cause the liquefied first gas to flow into an upstream side of the pump in the second path, a cooling heat exchanger configured to cool the first gas by a second low-temperature liquefied gas or a second gas being disposed in the reliquefaction path.

The invention relates to a system for supplying a gaseous fuel that comprises a low temperature tank for receiving the fuel in its liquid aggregate state achieved by cooling and comprises a rail that is fluidically connected to at least one injector device for discharging gaseous fuel into a combustion space. The system is characterized in that it has a pressure store that is configured to receive gaseous fuel and that is fluidically connectable to both the low temperature tank and the rail to buffer fuel coming from the low temperature tank and to supply it to the rail.

A system supplies gas to a high-pressure gas-consuming apparatus and a low-pressure gas-consuming apparatus of a floating structure including a tank. The supply system includes: a first supply circuit, a second supply circuit, a return line, a first heat exchanger and a second heat exchanger. The return line includes a flow-regulating member. The supply system includes a device for managing the supply system which includes a control module to control the flow-regulating member based on the characteristics of the gas.

A method and system for forming a compressed gas and dispensing it to a compressed gas receiver. The compressed gas is formed from a process fluid provided at a cryogenic temperature. The forming includes pressurizing the process fluid, feeding the pressurized process fluid at still a cryogenic temperature to a heat exchanger and heating it in indirect heat exchange with a thermal fluid which is provided in a reservoir at a thermal fluid temperature above the cryogenic temperature of the pressurized process fluid. Once heated to a suitable temperature the compressed gas may be dispensed to the compressed gas receiver or stored in one or more compressed gas storage vessels for later use.

A dry vaporizer, the dry vaporizer including a plurality of passages for accommodating a heating means each, at least two channels passing through the body wherein the channels are configured for passing a vaporized fluid, and a thermostat expansion valve configured to operate based on temperature of the body. The heating means are removable heaters placed in three passages of the body arranged in an equilateral triangle to enable equal heat distribution in the body and a method thereof.

An apparatus to refuel a vessel with cryo-compressed hydrogen is disclosed herein. The apparatus includes a refueler controller configured to defuel the vessel prior to a refuel process based on a pressure of the vessel; fill a mixing tank with at least the cryo-compressed hydrogen based on the pressure of the vessel and a pressure of the mixing tank, wherein the mixing tank is connected upstream of the vessel and is structured to include the cryo-compressed hydrogen; initiate the refuel process of the vessel; adjust a temperature of the mixing tank in response to a temperature of the vessel not satisfying a target temperature of the vessel during the refuel process, wherein the temperature of the mixing tank is to be adjusted based on an increase or a decrease of flow of supercritical hydrogen; and end the refuel process in response to the pressure of the vessel satisfying a target pressure of the vessel.

A flow control panel is configured to control a flow of fuel from a storage bank to a dispenser. The flow control panel includes input and output flow controllers, and input and output ports, each output port coupled to a respective dispenser port. Each output flow controller is coupled to a respective input port and a respective output port, and is configured to enable the flow of fuel from the input port and the output port. A processor is configured to control the input flow controllers and the output flow controllers. The processor is coupled to a memory storing instructions that when executed by the processor cause the processor to: receive a desired fuel pressure value from a dispenser; receive indications of fuel pressures within each of the storage banks; select a desired storage bank having the lowest fuel pressure among the storage banks that have fuel pressures greater than the desired fuel pressure; and activate a desired input port and a desired output port to enable fluid flow from the desired storage bank to the dispenser.

A flow control panel is configured to control a flow of fuel from a storage bank to a dispenser. The flow control panel includes input and output flow controllers, and input and output ports, each output port coupled to a respective dispenser port. Each output flow controller is coupled to a respective input port and a respective output port, and is configured to enable the flow of fuel from the input port and the output port. A processor is configured to control the input flow controllers and the output flow controllers. The processor is coupled to a memory storing instructions that when executed by the processor cause the processor to: receive a desired fuel pressure value from a dispenser; receive indications of fuel pressures within each of the storage banks; select a desired storage bank having the lowest fuel pressure among the storage banks that have fuel pressures greater than the desired fuel pressure; and activate a desired input port and a desired output port to enable fluid flow from the desired storage bank to the dispenser.