Abstract: A dispenser of cooled or heated liquid which in one embodiment is a server cart for an aircraft. To avoid the need for a pump, the reservoir has a cooling or heating heat exchanger that helically coils around the main reservoir, which cools from the top down or heats from the bottom up, forming a counter current. The reservoir is connected to at least two conduits, one near the cooler top of the reservoir and one near the relatively warmer bottom of the reservoir. The two conduits connect to one another at a distance from the reservoir forming a dispensing passage, thereby allowing fluid to constantly circulate through the dispensing passage due to difference in the specific gravity in the fluid caused by the temperature difference. The elimination of the pump device is especially desirable for weight sensitive environments such as an aircraft.

Abstract: An apparatus and method for producing liquefied natural gas. A liquefaction plant may be coupled to a source of unpurified natural gas, such as a natural gas pipeline at a pressure letdown station. A portion of the gas is drawn off and split into a process stream and a cooling stream. The cooling stream passes through a turbo expander creating work output. A compressor is driven by the work output and compresses the process stream. The compressed process stream is cooled, such as by the expanded cooling stream. The cooled, compressed process stream is divided into first and second portions with the first portion being expanded to liquefy the natural gas. A gas-liquid separator separates the vapor from the liquid natural gas. The second portion of the cooled, compressed process stream is also expanded and used to cool the compressed process stream. Additional features and techniques may be integrated with the liquefaction process including a water clean-up cycle and a carbon dioxide (CO2) clean-up cycle.

Abstract: The invention comprises a system for supplying carbon dioxide liquids while maintaining a desirable pressure in a liquid carbon dioxide storage vessel. In an exemplary embodiment, an improved vaporizer is deployed in a downstream line from the storage vessel. The vaporizer converts a portion of the withdrawn liquid carbon dioxide into replacement carbon dioxide vapor using heat from steam or electricity supplied by the facility. This replacement carbon dioxide vapor is returned to the storage vessel to maintain the desired internal tank pressure as liquified carbon dioxide is withdrawn. The vaporizer includes an elongated cylindrical steel shell with spaced apart ends. Each end has a steel end cap that is welded to the body. Either end cap may be removed to service the vaporizer. The vaporizer body is penetrated by three ports, a steam inlet, a liquid carbon dioxide inlet and a carbon dioxide vapor outlet.

Abstract: The apparatus for the expansion of fluid in the gaseous or liquid state or in double phase is characterized in that it has an expansion compartment comprising:a first spiral (72),a second spiral (70) located within said first spiral,means (52, 63) to permit a circular translation movement without self-rotation of the second spiral within the first spiral during the expansion of a fluid.

Abstract: A high efficiency oxygen/air separation system uses waste heat produced by an internal combustion engine to produce pure or enriched oxygen for combustion in the internal combustion engine. Nitrogen is eliminated from the combustion process, thus preventing the formation of nitrogen oxides. The formation of other particulates is also reduced as the exhaust gases are repeatedly burned. The separation system includes a manifold heat exchanger, a vane compressor/expander, a spent nitrogen heat exchanger and an insulated container. Air is first compressed in the integrated vane compressor/expander. Compression energy is provided from the expansion of the spent nitrogen after that nitrogen has been heated to exhaust manifold temperatures. High efficiency is achieved through simultaneous expansion and compression. The compressed air is cooled through a spent nitrogen heat exchanger and enters the insulated container, where the oxygen separation takes place.