The present technology is directed to processes involving formation of hydrocarbons and oxygenated hydrocarbons through use of oxygen supplied by ion transport membranes. More particularly, the present technology relates in part to a process involving steam reforming and subsequent production of a synthetic product where carbon dioxide and/or hydrogen downstream of the process is reclaimed to generate the synthetic product. The present technology also relates in part to an ethylene formation process involving a viral-templated coupling catalyst in the presence of an ion transport membrane.

InGaN offers a route to high efficiency overall water splitting under one-step photo-excitation. Further, the chemical stability of metal-nitrides supports their use as an alternative photocatalyst. However, the efficiency of overall water splitting using InGaN and other visible light responsive photocatalysts has remained extremely low despite prior art work addressing optical absorption through band gap engineering. Within this prior art the detrimental effects of unbalanced charge carrier extraction/collection on the efficiency of the four electron-hole water splitting reaction have remained largely unaddressed. To address this growth processes are presented that allow for controlled adjustment and establishment of the appropriate Fermi level and/or band bending in order to allow the photochemical water splitting to proceed at high rate and high efficiency. Beneficially, establishing such material surface charge properties also reduces photo-corrosion and instability under harsh photocatalysis conditions.

A system and method for performing plasma reactions creating a plasma area in a gas adjacent to a liquid. An embodiment of the plasma reactor includes a housing with an internal reaction chamber, first and second inlet paths to the reaction chamber, and electrodes for producing an electric field. The system may optionally further include a pre-ionization electrode and pre-ionization electric field for pre-ionizing a feed gas prior to entry into a reaction chamber. The reactor uses plasma to ionize gas adjacent with the liquid. The ionized gas reacts with the liquid to form an effluent. Exemplary uses of the plasma reactor include ionic injection, gas dissociation, liquid re-formation, and liquid dissociation. An alternative embodiment provides a system and method for infusion of gaseous particles into liquid by applying an electric field at power levels lower than the voltage required to form a plasma to gas adjacent to liquid.

A system and method for performing plasma reactions creating a plasma area in a gas adjacent to a liquid. An embodiment of the plasma reactor includes a housing with an internal reaction chamber, first and second inlet paths to the reaction chamber, and electrodes for producing an electric field. The system may optionally further include a pre-ionization electrode and pre-ionization electric field for pre-ionizing a feed gas prior to entry into a reaction chamber. The reactor uses plasma to ionize gas adjacent with the liquid. The ionized gas reacts with the liquid to form an effluent. Exemplary uses of the plasma reactor include ionic injection, gas dissociation, liquid re-formation, and liquid dissociation. An alternative embodiment provides a system and method for infusion of gaseous particles into liquid by applying an electric field at power levels lower than the voltage required to form a plasma to gas adjacent to liquid.

A device for producing purified oxygen, has a feed (1, 1′) of a mixture of oxygen and argon, and has at least one bed (2, 2A, 2B) of oxygen adsorption material, a purge (3, 3′) for discharging the separated argon and a circuit (4, 4′) for injecting a portion of the purified oxygen produced, into the feed (1, 1′). The device has a programmable logic controller (PLC) for treating the degree of purity and/or the production flow rate that can be set by the user and a control of said purge (3, 3′) as a function of the degree of purity of the purified oxygen and/or of the production flow rate which are desired by the user.

An electromagnetic resonance apparatus for molecular, atomic, and chemical modification of water is provided. The apparatus includes a water container, a resonance induction cell tower, an electronic control unit, a 12-volt power source, a DC to AC power inverter, and a pressure vessel for storing produced hydrogen gas. An electronic control unit is used to provide vibrational energy to the cell tower to facilitate water decomposition.

This invention relates to a method and apparatus for recycling plastics, electronics, munitions or propellants. In particular, the method comprises reacting a feed stock with a molten aluminum or aluminum alloy bath. The apparatus includes a reaction vessel for carrying out the reaction, as well as other equipment necessary for capturing and removing the reaction products. Further, the process can be used to cogenerate electricity using the excess heat generated by the process.

A process of producing a feed form a solid electrolyte oxygen separator and combusting the feed in a steam methane reforming furnace to produce a flue gas.

An oxygen concentrator is provided with a controller for recovering an oxygen concentration to a level suitable for treatment in a short period of time by selecting an optimum purge time corresponding to the deterioration state of an adsorbent. The judgment of moisture-absorption deterioration is performed when the detected value of the oxygen concentration sensor is equal to or less than a control value of the oxygen concentration in the oxygen-enriched gas and the detected value of the pressure sensor is equal to or more than an adsorption pressure at which the oxygen concentration increases significantly before and after the control to reduce the purge time, and control of reducing a time for the purge step shorter than a preset time is performed.

An oxygen concentrator is provided with a controller for recovering an oxygen concentration to a level suitable for treatment in a short period of time by selecting an optimum purge time corresponding to the deterioration state of an adsorbent. The judgment of moisture-absorption deterioration is performed when the detected value of the oxygen concentration sensor is equal to or less than a control value of the oxygen concentration in the oxygen-enriched gas and the detected value of the pressure sensor is equal to or more than an adsorption pressure at which the oxygen concentration increases significantly before and after the control to reduce the purge time, and control of reducing a time for the purge step shorter than a preset time is performed.