The present invention describes an improved process for the commercial scale production of high-quality catalyst materials. These improved processes allow for production of catalysts that have very consistent batch to batch property and performance variations. In addition these improved processes allow for minimal production losses (by dramatically reducing the production of fines or small materials as part of the production process). The improved process involves multiple steps and uses calcining ovens that allow for precisely control temperature increases where the catalyst is homogenously heated. The calcining gas is released into a separate heating chamber, which contains the recirculation fan and the heat source. Catalysts that may be produced using this improved process include but are not limited to catlaysts that promote CO hydrogenation, reforming catalysts, Fischer Tropsch Catalysts, Greyrock GreyCat™ catalysts, catalysts that homologate methanol, catalysts that promote hydrogenation of carbon compounds, and other catalysts used in industry.

A multi-chamber type heating unit to heat a blank includes: a lower housing unit; an intermediate housing unit installed in an upper portion of the lower housing unit; and an upper housing unit installed in an upper portion of the intermediate housing unit. A plurality of intermediate housings are stacked to form the intermediate housing unit, and a heating unit to heat a blank is installed in each of the intermediate housings. Moreover, the intermediate housings are formed in the shape in which upper and lower portions thereof are opened, and an opening is formed in the front for a door to be inserted thereinto, and door sealing units provided on the intermediate housing portion and provided to seal the door when the door is closed.

The present invention is directed to an oil-line assembly for an oil-fired boiler or furnace having a hinged door, the oil-line assembly includes a bracket, an elongated pipe, a first socket, a second socket, and a flexible hose. The bracket having a first plate member, a second plate member, the first plate member and a second plate member having a common edge. The elongated pipe member coupled to an edge opposite the common edge of the second plate member, the elongated pipe member extends along its longitudinal axis which runs parallel to the common edge, the elongated pipe member having a proximal end and a distal end; The first socket secured to the proximal end of the elongated pipe member. The free end of the first socket is configured to receive an oil-line that extends from an oil source. The second socket coupled to the distal end of the elongated pipe member. The flexible hose having a proximal end and a distal end, wherein the proximal end of the flexible hose is coupled to a free end of the second socket, the distal end of the flexible hose configured to couple to an input of the oil-fired heating unit.

A shaft furnace, in particular a blast furnace, includes a metal jacket defining the furnace outer wall and a protective layer protecting the inner surface of the outer wall. At least one condition monitoring probe is arranged inside within the protective layer to monitor the latter. The condition monitoring probe is connected to a wireless module arranged outside the outer wall to transmit condition monitoring data. The wireless module is located inside a casing mounted to the outer surface of the metal jacket. The condition monitoring probe includes one or more conductive loops positioned at predetermined depths below the front face of the cooling plate body, or of the refractory lining, so that wear of the body, resp. refractory, can be detected by a change of an electrical characteristic of the loop(s) due to abrasion.

A gas phase type heating method includes loading an object into a vapor heating furnace or a heating furnace via a loading/unloading portion, cooling vapor of a heat transfer liquid by a cooler provided above the loading/unloading portion in the vapor heating furnace, and causing a gas to go in and out, making a pressure in a continuous furnace uniform, and heating the loaded object, by a connection portion that is provided above the cooler and has a pressure loss smaller than a pressure loss of the loading/unloading portion.

A tube arrangement comprising a first metal tube, a second metal tube, a first sleeve part, and a second sleeve part. The first and second sleeve parts are threadedly connected to the first and second metal tubes. The first and second metal tubes are configured to be joined via a butt weld joint. The first sleeve and the second sleeve are configured to be joined via a second butt weld joint. The first sleeve part comprises a first outer surface extending at a first acute angle () to an axial centre axis of the first sleeve part and the second sleeve part comprises a second outer surface extending at a second acute angle () to an axial centre axis of the second sleeve part. The present disclosure also relates to a furnace.

The present invention describes an improved process for the commercial scale production of high-quality catalyst materials. These improved processes allow for production of catalysts that have very consistent batch to batch property and performance variations. In addition these improved processes allow for minimal production losses (by dramatically reducing the production of fines or small materials as part of the production process). The improved process involves multiple steps and uses calcining ovens that allow for precisely control temperature increases where the catalyst is homogenously heated. The calcining gas is released into a separate heating chamber, which contains the recirculation fan and the heat source. Catalysts that may be produced using this improved process include but are not limited to catalysts that promote CO hydrogenation, reforming catalysts, Fischer Tropsch Catalysts, Greyrock GreyCat? catalysts, catalysts that homologate methanol, catalysts that promote hydrogenation of carbon compounds, and other catalysts used in industry.

A semiconductor high pressure annealing device is described. The semiconductor high pressure annealing device includes a chamber body, a cover, a lifting mechanism, and a floating sealing structure. Air tightness between the chamber body and the cover is achieved by the floating sealing structure. A first sealing ring and a second sealing ring of the floating sealing structure are arranged on the top and the bottom for reducing the damage to the first sealing ring and the second sealing ring when the cover moves up and down. A preload spring assembly of the floating sealing structure can provide tension to assist in improving the air tightness between the chamber body and the cover.

A graphite purification system contains a vessel adapted to contain graphite particles, including an inductive coil for heating said vessel; and a cooling system for cooling said graphite purification system, whereby the cooling system is adapted to also cool the graphite particles. The purification system may be a continuous or batch system, and, the vessel may be at least partially formed from graphite. A process for purifying graphite particles is also presented and includes providing a vessel formed at least partially from graphite; loading graphite particles into the vessel; inductively heating at least a portion of the vessel, and thereby heating the graphite particles in physical contact with the vessel; and cooling the vessel and the graphite particles.

The present invention describes an improved process for the commercial scale production of high-quality catalyst materials. These improved processes allow for production of catalysts that have very consistent batch to batch property and performance variations. In addition these improved processes allow for minimal production losses (by dramatically reducing the production of fines or small materials as part of the production process). The improved process involves multiple steps and uses calcining ovens that allow for precisely control temperature increases where the catalyst is homogenously heated. The calcining gas is released into a separate heating chamber, which contains the recirculation fan and the heat source. Catalysts that may be produced using this improved process include but are not limited to catlaysts that promote CO hydrogenation, reforming catalysts, Fischer Tropsch Catalysts, Greyrock GreyCat? catalysts, catalysts that homologate methanol, catalysts that promote hydrogenation of carbon compounds, and other catalysts used in industry.