Patent classifications
B01J2219/0883
Apparatus and Method for Generating Nitric Oxide in Controlled and Accurate Amounts
A nitric oxide generator generates nitric oxide from a mixture of nitrogen and oxygen such as air treated by a pulsating electrical discharge. The desired concentration of nitric oxide is obtained by controlling at least one of a frequency of the pulsating electrical discharge and duration of each electrical discharge pulse.
METHOD FOR SYNTHESISING CORE-SHELL SILICON-GERMANIUM NANOPARTICLES BY LASER PYROLYSIS, METHOD FOR PRODUCING AN ELECTRODE FOR A LITHIUM BATTERY AND ASSOCIATED ELECTRODE
Provided is method for synthesising core-shell nanoparticles by laser pyrolysis. The method may include a) conveying together a gaseous mixture including a silicon precursor and a germanium precursor in a reaction zone of a first chamber of a reactor, and b) emitting a first laser beam at the level of the reaction zone for carrying out a laser pyrolysis of the mixture, the steps making it possible to obtain nanoparticles having a core made of a silicon- and germanium-based alloy and a silicon shell.
Apparatus and Method for Generating Nitric Oxide in Controlled and Accurate Amounts
A nitric oxide generator generates nitric oxide from a mixture of nitrogen and oxygen such as air treated by a pulsating electrical discharge. The desired concentration of nitric oxide is obtained by controlling at least one of a frequency of the pulsating electrical discharge and duration of each electrical discharge pulse.
Method for treating sulfur hexafluoride using radiation and apparatus for collecting and treating by-products
Provided are a method for treating sulfur hexafluoride and an apparatus for collecting and treating by-products. The method for treating sulfur hexafluoride, and the apparatus for collecting and treating by-products according to the present invention are a significantly effective method and apparatus capable of safely treating sulfur hexafluoride at low cost.
PLASMA POLYMERISATION APPARATUS
Plasma polymerisation apparatus is disclosed including a reaction zone and at least one gas inlet for supplying at least one monomer in a gaseous form to the reaction zone, a first electrode and a second electrode spaced apart and configured to generate an electric field in the reaction zone to form plasma polymer nanoparticulate material from the at least one monomer, a plurality of collectors configured to collect plasma-polymer nanoparticulate material formed in the reaction zone, the plurality of collectors being located adjacent the second electrode, and a cooling device located adjacent the second electrode and configured to cool the plurality of collectors. Also disclosed is plasma polymerisation apparatus that includes a confinement grid extending between a first electrode and a second electrode of the apparatus.
COMPLEX MODALITY REACTOR FOR MATERIALS PRODUCTION AND SYNTHESIS
Disclosed apparatuses, systems, and materials relate to the disassociation of feedstock species (such as those in gaseous form) into constituent components, and may include an energy generator configured to provide a microwave energy. A first chamber defines a first volume and is configured to guide the microwave energy along the first chamber as a sinusoidal wave having an energy maxima at a point along the first chamber. A second chamber contains a plasma plume and is positioned substantially proximal to the first chamber, and is configured to enable propagation of the microwave energy through the first chamber and the second chamber such that the microwave energy demonstrates, at a radial center of the second chamber, a coaxial energy maxima configured to ignite the plasma plume contained in the second chamber. Carbon-containing materials may be formed by controlling flow parameters of the feedstock species into the first or second chamber.
Solar thermochemical processing system and method
A solar thermochemical processing system is disclosed. The system includes a first unit operation for receiving concentrated solar energy. Heat from the solar energy is used to drive the first unit operation. The first unit operation also receives a first set of reactants and produces a first set of products. A second unit operation receives the first set of products from the first unit operation and produces a second set of products. A third unit operation receives heat from the second unit operation to produce a portion of the first set of reactants.
Apparatus and method for generating nitric oxide in controlled and accurate amounts
A nitric oxide generator generates nitric oxide from a mixture of nitrogen and oxygen such as air treated by a pulsating electrical discharge. The desired concentration of nitric oxide is obtained by controlling at least one of a frequency of the pulsating electrical discharge and duration of each electrical discharge pulse.
Process for the partial oxidation of fuels and the device for applying said process
The invention comprises a process for obtaining a gas from a fluid fuel and an oxidising fluid, said process comprising steps in which the incoming fluid is subjected to temperature, photocatalytic action and reaction with catalysts, all this within a device with a tubular structure which the incoming fluid circulates through in a spiral manner, between a fixed bed attached to the walls of the duct and a circulating bed with an ionised gas stream that occupies a central position of the duct, producing a gas obtained.
Method and apparatus for synthesizing methane gas from carbon dioxide and hydrogen at room temperature and atmospheric pressure
A methane (CH.sub.4) gas is synthesized from carbon dioxide (CO.sub.2) and hydrogen (H.sub.2) using catalyst-dielectric barrier discharge (DBD) plasma at room temperature and atmospheric pressure. In the method and apparatus for synthesizing methane gas of the invention, methane (CH.sub.4) gas, which is synthetic natural gas, can be effectively synthesized only from carbon dioxide (CO.sub.2) and hydrogen (H.sub.2) using DBD plasma at room temperature and atmospheric pressure, and also, additional heating and pressurization devices are not used during the methane gas synthesis process, thus reducing production costs and realizing high-value-added processing due to the absence of risks during the processing.