A catalyst structure, which makes it possible to reduce the flow passage resistance and raise the purification rate, is provided. A catalyst structure provided in an exhaust passage of an internal combustion engine comprises a base member which is formed by combining wire-shaped members, wherein the wire-shaped members do not include any wire-shaped member which is arranged to be orthogonal to a flow direction of an exhaust gas, and the wire-shaped members include wire-shaped members which are arranged obliquely with respect to the flow direction of the exhaust gas. The change in the cross-sectional area of the base member is suppressed by arranging the wire-shaped members obliquely with respect to the flow direction of the exhaust gas.

A device for making a carbon nanotube array includes a chamber, a gas diffusing unit and a gas supplying pipe. The gas diffusing unit and the gas supplying pipe are in the chamber. The gas diffusing unit is a hollow structure and defines a hole and an outlet. The gas supplying pipe includes a first end and a second end opposite to the first end. The first end extends out of the chamber. The second end is in the chamber and connected to the hole.

Methane may be dissociated at low temperatures and/or pressures utilizing a reactor designed to generate shockwaves in a supersonic gaseous vortex. Within a preprocessing chamber, the methane may be pressurized to a pressure of 700 kPa or more, and heated to a temperature below a dissociation temperature of methane. The methane may be introduced as a gas stream substantially tangentially to an inner surface of a chamber of the reactor to effectuate a gaseous vortex rotating about a longitudinal axis within the chamber. The gas stream may be introduced using a nozzle that accelerates the gas stream to a supersonic velocity. A frequency of shockwaves emitted from the nozzle into the gaseous vortex may be controlled. Product gas and carbon byproduct may be emitted from the chamber of the reactor. The carbon byproduct may be separated out from the product gas using a gas/solid separator.

The invention relates to a structured catalyst for catalyzing steam methane reforming reaction in a given temperature range T upon bringing a hydrocarbon feed gas into contact with the structured catalyst. The structured catalyst comprises a macroscopic structure, which comprises an electrically conductive material and supports a ceramic coating. The macroscopic structure has been manufactured by 3D printing or extrusion and subsequent sintering, wherein the macroscopic structure and the ceramic coating have been sintered in an oxidizing atmosphere in order to form chemical bonds between the ceramic coating and the macroscopic structure. The ceramic coating supports catalytically active material arranged to catalyze the steam methane reforming reaction, wherein the macroscopic structure is arranged to conduct an electrical current to supply an energy flux to the steam methane reforming reaction. The invention moreover relates to methods of manufacturing the structured catalyst and a system using the structured catalyst.

The disclosure relates to systems and methods that include using a plurality of reactors for the conversion of a stream of ammonia (NH.sub.3) to hydrogen (H.sub.2) and nitrogen (N.sub.2). The stream of ammonia is heated prior to introduction into each reactor. The reactors can be adiabatically operated.

The disclosure relates to solar-based reactor tubes and related systems and methods. In general, the reactor tube includes an exterior cylinder, a cylindrical hydrogen-permeable membrane disposed in an interior space of the exterior cylinder, an annular space defined by an outer surface of the cylindrical hydrogen-permeable membrane and an inner surface of the exterior cylinder, a catalyst, and a heating element. A first gas stream and a second gas stream can be configured to pass through the reactor tube. The systems can be used to produce hydrogen (e.g., from ammonia cracking).

The present disclosure relates to a single shell open interstage reactor (SSOI). The SSOI comprises a first reaction stage, an interstage heat exchanger, an open interstage region, and a second reaction stage. The SSOI may be configured for upflow or downflow operation. Further, the open interstage region of the SSOI may comprise a supplemental oxidant feed. When the open interstage region comprises a supplemental oxidant feed, the SSOI may further comprise a supplemental oxidant mixing assembly. Processes for producing acrylic acid through the oxidation of propylene are also disclosed.

A method for producing a carbon nanostructure according to an aspect of the present invention is a method in which a carbon nanostructure is produced between a base body and a separable body while the separable body is relatively moved away from the base body, the base body including a carburizable metal that is a principal constituent, the separable body including a carburizable metal that is a principal constituent, the separable body being joined to or in contact with the base body in a linear or strip-like shape. The method includes a carburizing gas feed step, an oxidizing gas feed step, a heating step in which the portion of the base body at which the base body and the separable body are joined to or in contact with each other is heated, and a separation step in which the separable body is relatively moved away from the base body.

A water gas shift (WGS) reactor system includes a housing; a reaction tube disposed in the housing, wherein a reaction channel is defined within the reaction tube and a cooling fluid channel is defined between the housing and the reaction tube; a catalyst disposed in the reaction channel, the catalyst configured to catalyze a hydrogen generation reaction; and a heat transfer material disposed in the reaction channel.

The invention relates to a reactor for cracking hydrocarbons wherein the reactor has inner wall; characterized in that the inner wall comprises a plurality of concave dimples embedded in a surface of said inner wall.