A system to prevent the formation of hydrates in a pipeline includes a heater assembly. The heater assembly has a vortex tube mounted on an outer surface of a first section of the pipeline and a compressed gas source. The vortex tube is configured to separate gas from an inlet into a hot gas pathway and a cold gas pathway. The vortex tube includes an inlet, a cold gas outlet, and a hot gas outlet. The hot gas outlet of the vortex tube is fluidly connected to an opening defined in the first section of the pipeline. The hot gas outlet is configured to flow hot gas from the vortex tube into an interior volume of the pipeline. The compressed gas source is fluidly connected to the inlet of the vortex tube.

A device equipped with a tank, includes: the tank to be filled with a fuel gas; a valve mechanism provided in the tank; a receptacle with which a nozzle of a fuel gas filling device is connectable; a first filling path, an upstream end of the first filling path communicating with the receptacle; a second filling path, a downstream end of the second filling path communicating with the tank through the valve mechanism; and a storage container hermetically communicating between a downstream end of the first filling path and an upstream end of the second filling path, and storing foreign matter contained in the fuel gas, wherein the storage container is positioned vertically above the downstream end of the first filling path.

An integrated hydrogen fueling station for fueling of vehicle tanks with hydrogen comprising an electrochemical compressor in which secondary hydrogen originating from leakage, boiling-off or venting of hydrogen-containing gas in one or more mechanical hydrogen compressors is collected and transferred to the electrochemical compressor and compressed by the electrochemical compressor, wherein the secondary hydrogen contains hydrogen and further gaseous components. A method for operating a hydrogen fueling station for fueling of vehicle tanks with hydrogen wherein secondary hydrogen originating from leakage, boiling-off or venting of hydrogen-containing gas in one or more mechanical hydrogen compressors of the fueling station operative units is collected and transferred to an electrochemical compressor and compressed in the electrochemical compressor, and wherein the secondary hydrogen contains hydrogen and further gaseous components.

A system to prevent the formation of hydrates in a pipeline includes a heater assembly. The heater assembly has a vortex tube mounted on an outer surface of a first section of the pipeline and a compressed gas source. The vortex tube is configured to separate gas from an inlet into a hot gas pathway and a cold gas pathway. The vortex tube includes an inlet, a cold gas outlet, and a hot gas outlet. The hot gas outlet of the vortex tube is fluidly connected to an opening defined in the first section of the pipeline. The hot gas outlet is configured to flow hot gas from the vortex tube into an interior volume of the pipeline. The compressed gas source is fluidly connected to the inlet of the vortex tube.

Methods and systems for recompression are disclosed. In certain embodiments, a method may include receiving a fluid from a first conduit or container at a first pressure. The method may include using a multi-stage compressor which is non-removably mounted to a trailer to compress the fluid through one or more compression stages. The method may include cooling the fluid after each stage of compression, scrubbing liquid from the fluid before each stage of compression, and discharging the fluid to a second conduit or container at a second pressure.

Nitrox-mixtures production machine comprising: a molecular separator, which is structured so as to receive at inlet a flow of air and to provide at outlet an intermediate Nitrox mixture with high oxygen percentage; a low-pressure compressor, which is adapted to feed an airflow at inlet of the molecular separator; a mixing manifold, which communicates with the molecular separator so as to receive said intermediate Nitrox mixture, and is structured so as to mix the intermediate Nitrox mixture with fresh air coming from the outside, in order to provide at outlet a final Nitrox mixture with predefined composition; at least one oxygen sensor, which is adapted to measure the oxygen percentage present in said final Nitrox mixture; at least one pressure sensor, which is adapted to measure the air pressure in the molecular separator; and an electronic control device, which is connected to said at least one oxygen sensor and is adapted to regulate the flowrate of the airflow that is sucked in by the low-pressure compressor based on the signals coming from said at least one oxygen sensor and said at least one pressure sensor.

Nitrox-mixtures production machine comprising: a molecular separator, which is structured so as to receive at inlet a flow of air and to provide at outlet an intermediate Nitrox mixture with high oxygen percentage; a low-pressure compressor, which is adapted to feed an airflow at inlet of the molecular separator; a mixing manifold, which communicates with the molecular separator so as to receive said intermediate Nitrox mixture, and is structured so as to mix the intermediate Nitrox mixture with fresh air coming from the outside, in order to provide at outlet a final Nitrox mixture with predefined composition; at least one oxygen sensor, which is adapted to measure the oxygen percentage present in said final Nitrox mixture; and an electronic control device, which is connected to said at least one oxygen sensor and is adapted to regulate the flowrate of the airflow that the low-pressure compressor feeds at inlet of the molecular separator based on the signals coming from said at least one oxygen sensor.

A compressed natural gas storage and dispensing system having descending pressure bulk storage banks in fluid communication with a supply source for CNG and high pressure storage banks in fluid communication with the descending pressure bulk storage bank, both banks being in fluid communication with fuel dispensers, wherein the delivery pressure of the CNG during simultaneous refueling of CNG powered vehicles is equalized.

A method of transporting natural gas by liquefaction of natural gas at ambient temperature, achieved by mixing the natural gas at high pressure with a hydrocarbon that is a stable liquid at ambient temperature and ambient pressure. The hydrocarbon liquid may be crude oil or a distillate of crude oil. The method includes: liquefaction: mixing the natural gas with the hydrocarbon liquid at an ambient temperature and a high pressure to generate a liquid mixture, which contains the natural gas dissolved in the hydrocarbon liquid; shipping: transporting the liquid mixture using a marine tanker, during which the liquid mixture is maintained at ambient temperature and the high pressure; and regasification: at the destination, releasing a gas from the liquid mixture by lowering the pressure of the liquid mixture. The hydrocarbon liquid may be used multiple times.

A system and method for supplying a backup product in an air separation device, as well as a system and method for supplying a lower-pressure product to a user by means of pressurization of a cryogenic liquid pump during normal operation of an air separation device, i.e., when the cryogenic liquid pump is in the cold standby state. By means of the system and method, a cryogenic liquid product taken from a storage tank is pressurized by the cryogenic liquid pump to produce a lower-pressure product by taking full advantage of the low-speed operation of the cryogenic liquid pump in the cold standby state, and the lower-pressure product is transmitted to product supply lines of a user, to achieve the function of supplying the lower-pressure product to the user. The system and method not only reduce the energy loss of the cryogenic liquid pump in the cold standby state for a long time, but also avoid the bleeding rate of the cryogenic liquid product generated by sending a part of the cryogenic liquid product back to the storage tank, so that the advantage of quickly starting the cryogenic liquid pump from the cold standby state is ensured, and the requirements of the user to the higher-pressure product and the lower-pressure product can be satisfied.