Abstract: A system to place one or more rovings made from composite material on a substrate. The system includes at least a roving-laying head configured to lay at least one roving, an electricity generator and at least one plasma torch. The plasma torch mounted on the roving-laying head and powered by the electricity generator. The plasma torch being further supplied with at least one plasma-forming fluid to generate at least one plasma jet suitable for heating the one or more rovings to be laid on the substrate.

Abstract: A plasma cutting method providing a plasma torch having an electrode disposed within a first nozzle with a first exit section facing an end of the electrode. The first gas source supplies a gas to the first nozzle. A second nozzle is arranged concentrically around the first nozzle and has a second exit section substantially facing the first exit section. A second gas source supplies the gas between the first nozzle and the second nozzle. The electrode is supplied with a current, and the first and second nozzles are supplied with the gas to form a plasma with the gas introduced into the first nozzle. The surrounding pressure around the plasma jet in the second nozzle at the exit of the first nozzle is controlled to be at least superior to the atmospheric pressure and inferior to the pressure in the first exit section.

Abstract: A system to place one or more rovings made from composite material on a substrate. The system includes at least a roving-laying head configured to lay at least one roving, an electricity generator and at least one plasma torch. The plasma torch mounted on the roving-laying head and powered by the electricity generator. The plasma torch being further supplied with at least one plasma-forming fluid to generate at least one plasma jet suitable for heating the one or more rovings to be laid on the substrate.

Abstract: A plasma cutting method providing a plasma torch having an electrode disposed within a first nozzle with a first exit section facing an end of the electrode. The first gas source supplies a gas to the first nozzle. A second nozzle is arranged concentrically around the first nozzle and has a second exit section substantially facing the first exit section. A second gas source supplies the gas between the first nozzle and the second nozzle. The electrode is supplied with a current, and the first and second nozzles are supplied with the gas to form a plasma with the gas introduced into the first nozzle. The surrounding pressure around the plasma jet in the second nozzle at the exit of the first nozzle is controlled to be at least superior to the atmospheric pressure and inferior to the pressure in the first exit section.

Abstract: A furnace for performing an endothermic process comprising tubes containing a catalyst for converting a gaseous feed, wherein tubes are positioned in rows inside the furnace, wherein burners are mounted between the tubes and between the tubes and the furnace walls parallel to the tubes row and wherein the burners rows and the tubes rows are ended by end walls and are divided into sections with the distance from the end burner to the end wall being B2W, the distance between two adjacent burners in the section being B2B, and half the distance in-between two sections being B2S, wherein the burners in the rows are arranged in such a way that the ratios B2B/B2W and B2B/B2S are greater than 1.3 thus limiting the occurrence of the flame merging phenomenon and reducing significantly the quadratic mean of the tube temperature profile.

Abstract: A furnace for performing an endothermic process comprising tubes containing a catalyst for converting a gaseous feed, wherein tubes are positioned in rows inside the furnace, wherein burners are mounted between the tubes and between the tubes and the furnace walls parallel to the tubes row and wherein the burners rows and the tubes rows are ended by end walls and are divided into sections with the distance from the end burner to the end wall being B2W, the distance between two adjacent burners in the section being B2B, and half the distance in-between two sections being B2S, wherein the burners in the rows are arranged in such a way that the ratios B2B/B2W and B2B/B2S are greater than 1.3 thus limiting the occurrence of the flame merging phenomenon and reducing significantly the quadratic mean of the tube temperature profile.

Abstract: A furnace for performing an endothermic process comprises tubes containing a catalyst for converting a gaseous feed, said tubes positioned inside the furnace, inner burners mounted to a furnace roof between the tubes, and outer burners mounted to the furnace roof between the tubes and a furnace wall. The outer burners are positioned close to the furnace wall, and configured to operate with 45-60% of the power of the inner burners and with an inlet velocity between 90 to 110% of the inlet velocity of the inner burners.

Abstract: A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, preferably natural gas, includes one or more helically coiled heat exchanger tubes which are arranged within a catalyst bed of a reforming catalyst and are helically coiled over part of their length located within the catalyst bed and are otherwise straight are present, where the straight proportion of the heat exchanger tubes and/or the helix pitch of the helically coiled part alters within the catalyst bed and matching to requirements of the pressure drop, the heat exchange properties, and the corrosion resistance.

Abstract: A furnace for performing an endothermic process comprises tubes containing a catalyst for converting a gaseous feed, said tubes positioned inside the furnace, inner burners mounted to a furnace roof between the tubes, and outer burners mounted to the furnace roof between the tubes and a furnace wall. The outer burners are positioned close to the furnace wall, and configured to operate with 45-60% of the power of the inner burners and with an inlet velocity between 90 to 110% of the inlet velocity of the inner burners.

Abstract: A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, preferably natural gas, includes one or more helically coiled heat exchanger tubes which are arranged within a catalyst bed of a reforming catalyst and are helically coiled over part of their length located within the catalyst bed and are otherwise straight are present, where the straight proportion of the heat exchanger tubes and/or the helix pitch of the helically coiled part alters within the catalyst bed and matching to requirements of the pressure drop, the heat exchange properties, and the corrosion resistance.

Abstract: In one embodiment, a method for generating heat energy includes injecting a stream having a concentration of at least 50% oxygen (O2 stream) into a primary gas stream through a mixer, the mixer discharging the O2 stream as two or more spaced jets traversing the primary stream, thereby enriching the primary gas stream. The method further includes mixing fuel with the enriched primary gas stream, thereby forming a fuel stream; and combusting the fuel stream, thereby forming a flue gas stream.

Abstract: In one embodiment, a method for generating heat energy includes injecting a stream having a concentration of at least 50% oxygen (O2 stream) into a primary gas stream through a mixer, the mixer discharging the O2 stream as two or more spaced jets traversing the primary stream, thereby enriching the primary gas stream. The method further includes mixing fuel with the enriched primary gas stream, thereby forming a fuel stream; and combusting the fuel stream, thereby forming a flue gas stream.

Abstract: In one embodiment, a method for generating heat energy includes injecting a stream having a concentration of at least 50% oxygen (O2 stream) into a primary gas stream through a mixer, the mixer discharging the O2 stream as two or more spaced jets traversing the primary stream, thereby enriching the primary gas stream. The method further includes mixing fuel with the enriched primary gas stream, thereby forming a fuel stream; and combusting the fuel stream, thereby forming a flue gas stream.

Abstract: In one embodiment, a method for generating heat energy includes injecting a stream having a concentration of at least 50% oxygen (O2 stream) into a primary gas stream through a mixer, the mixer discharging the O2 stream as two or more spaced jets traversing the primary stream, thereby enriching the primary gas stream. The method further includes mixing fuel with the enriched primary gas stream, thereby forming a fuel stream; and combusting the fuel stream, thereby forming a flue gas stream.

Abstract: The invention relates to an optical component (21), which can be used for the laser cutting of a material (26), comprising at least one aspherical refractive surface (22) shaped to focus the rays (30) of the incident beam onto a straight line segment (25) lying on the optical axis (29) of the optical component (21). The optical component (21) is of the transmissive type (21) or reflective type. For example, the optical element is formed by a lens (21) whose aspherical refractive surface (22) is defined by a radius of curvature (24) that varies continuously with the distance from the optical axis (29) of the lens. The laser beam is assisted by an assistance gas containing at least one component chosen from nitrogen, oxygen, helium, argon and mixtures thereof.