A nanostructure includes a plurality of substantially spherically curved carbon layers having diameters in a range of 1 nanometer to 1000 nanometers and a plurality of halogen atoms attached to an outer convex side of the carbon layers. A composition of matter includes a liquid fuel and an additive including at least one liquid and a plurality of carbon nano-onions. A method of fabricating an additive for liquid fuel includes creating a carbon-based material using a plasma in an environment including at least one hydrocarbon gas and/or at least one liquid containing hydrocarbons, organometallic metal-complex, and/or element-organic compounds, evaporating organic material from the carbon-based material, halogenating the carbon-based material, and extracting carbon nano-onions from the halogenated carbon-based material.

An apparatus for carrying out chemical reactions is provided. The apparatus comprises a first reactor/reaction zone for carrying out a first chemical reaction and a second reactor/reaction zone for carrying out a second chemical reaction. Each reactor/reaction zone comprises: a) an inner surface and an outer surface which are spaced apart from each other to define a reaction volume configured such that, in use, a respective chemical reaction takes place in the reaction volume, and wherein the inner surface and outer surface are configured for relative rotation with respect to each other, (b) an inlet for introduction of a reagent to the reaction volume, and (b) an outlet through which a reaction product can leave the reaction volume. The reaction products of the first reactor/reaction zone comprise reagents of the second reactor/reaction zone.

A method of substituting an azide for hydrogen bonded to a tertiary carbon atom is provided. A liquid mixture in an oxygen-free environment has spaced-apart carbon and platinum electrodes disposed therein. The liquid mixture includes a solvent, ammonium azide, and a base material having at least one tertiary carbon atom with hydrogen bonded thereto. An electric current is applied to the electrodes where the liquid mixture undergoes a reaction. The electrochemically-induced reaction yields a liquid product and a solid product. The liquid product includes the solvent and a constituent having at least one tertiary carbon atom with an azide bonded thereto.

In order to attain an efficient decomposition process by water plasma, a decomposition processor includes a water plasma generator which is configured to inject water plasma, from the injection port, by arc discharge generated between negative and positive electrodes; and a supply device configured to supply a decomposition target object to a water plasma jet stream injected from the water plasma generator, wherein the decomposition target object is decomposed by the water plasma. The supply device has a nozzle for providing the decomposition target object from a tip, and the negative electrode, the injection port, the positive electrode and the nozzle are arranged in that order along the center axis line of the injection port. The tip of the nozzle is placed inside of the water plasma jet stream.

In order to stabilize injection of water plasma, a vortex water flow generator forms a vortex water flow for passing arc discharge. The vortex water flow generator includes a cylindrical portion configured to form a vortex water flow along an inner circumference, a first middle partition and a second middle partition protruding from the inner circumference of the cylindrical portion. The first middle partition and the second middle partition respectively have an opening to include a center axis line position of the cylindrical portion. An opening of the second middle partition on the side of the positive electrode is larger than an opening of the first middle partition on the side of the negative electrode.

A vortex water generator forms a vortex water flow for passing arc discharge. The vortex water flow generator includes a cylindrical portion configured to form a vortex water flow along an inner circumference; first middle partition and second middle partition protruding from the inner circumference of the cylindrical portion, a rear partition formed in a rear end side of the cylindrical portion, and a front partition provided in a front end side of the cylindrical portion. Each partition has an opening to include a center axis line position of the cylindrical portion. Each opening has a different opening shape in size. The middle partition and the front partition have negative electrode side surfaces formed by tapered surfaces receding from the negative electrode as close to the center axis line. Arc-shaped beveled portions are formed between the tapered surfaces and inner circumferential surfaces of the openings.

A continuous flow catalytic reactor, an assembling method therefor and an application thereof includes a reaction vessel, a filler packaged in the reaction vessel and a charged catalytic component; the charged catalytic component is fixed to the filler under an action of a direct-current electric field. The continuous flow catalytic reactor may be applied to continuous flow reactions such as a monosaccharide epimerization reaction. A monosaccharide epimerization reaction method includes: providing the continuous flow catalytic reactor; electrically connecting the continuous flow catalytic reactor with a direct-current power supply, thereby to forming the direct-current electric field by electrically connecting the continuous flow catalytic reactor with the direct-current power supply; and heating a reactor container to a target temperature, and inputting a monosaccharide solution from a liquid flow inlet of the reaction vessel and then collecting a solution containing a target product from a liquid flow outlet of the reaction vessel.

Flow cell systems are provided. Example flow cell systems can include an H.sup.+/H.sub.2 half-cell and a counterpart Fe.sup.3+/Fe.sup.2+ or V.sup.5+/V.sup.4+ half-cell. Flow cell systems can also include a half-cell in fluid communication with an electrolyte regeneration chamber. Embodiments of these flow cells systems can be configured to produce hydrogen through electrolysis. Flow cell battery systems are also disclosed. Example flow cell battery systems can include an H.sup.+/H.sub.2 analyte; and a counterpart Fe.sup.3+/Fe.sup.2+ or V.sup.5+/V.sup.4+ catholyte. Processes for generating hydrogen are also disclosed. Example processes can include generating protons from a Fe.sup.3+/Fe.sup.2+ or V.sup.5+/V.sup.4+ electrolyte solution; and reacting the protons with H.sub.2O to form H.sub.2.

Systems and methods for a nitric oxide (NO) generation system are provided. In particular, the present disclosure provide an NO generation system that is configured to be cooled to maintain an NO generator of the system at or below temperatures safe for patient use and contact. In some non-limiting examples, the NO generation system may include a pump configured to furnish a fluid (e.g., a gas) toward and/or through the NO generator to provide cooling thereto.

A production apparatus and method for fine particles are capable of increasing a production amount and producing fine particles at low cost by efficiently inputting a large amount of material to plasma. The production apparatus includes a material supply device, which includes a plurality of material supply ports that supply a material gas containing material particles and are arranged below a plurality of electrodes in a vertical direction inside a vacuum chamber. The material supply device further includes a first gas supply port that supplies a first shield gas arranged in an inner periphery of the plural material supply ports and plural second gas supply ports that supply a second shield gas arranged in an outer periphery of the plural material supply ports.