Abstract:
A compressor generates compressed air. Iron powder is provided in a deoxidizing chamber. The compressed air is supplied to the deoxidizing chamber such that the compressed air reacts with the iron powder to form iron oxide, so that oxygen contained in the compressed air is reduced to obtain remained nitrogen gas.
Abstract:
A process is described in which an elastic fluid is contacted with a particulate solid. This comprises providing a substantially vertical elongate tubular containment zone (1) containing a charge of the particulate solid (5), the volume of the containment zone (1) being greater than the settled volume of the particulate solid (5). An upper retainer means (3) is mounted at the upper end of the containment zone (1), the upper retainer means (3) being permeable to the fluid but adapted to retain particulate solid (5) in the containment zone (1). A follower means (4) is movably mounted in the containment zone (1) beneath the charge of particulate solid (5) for movement upwardly from the lower end of the containment zone (1) upon upward flow of elastic fluid through the containment zone (1) at a rate beyond a threshold rate. In the process the elastic fluid is caused to flow upwardly through the containment zone (1) at a rate which is sufficient to cause particulate solid (5) to rise up towards the upper end of the containment zone and form a cushion of particulate solid (5) against the underside of the upper retainer means (3). This rate is in excess of the threshold rate so as to cause the follower means (4) to move upwardly until it abuts against the underside of the cushion of particulate solid (5). The invention also provides an apparatus suitable for carrying out such a process and a method of loading a particulate solid into a substantially vertical tube.
Abstract:
When a hydrogen producing apparatus is stopped, the flow rates of a hydrocarbon-type fuel feedstock, water and an oxygen-containing oxidant gas are decreased respectively. A random decrease of the flow rates, however, invites a rapid increase in the temperature of a catalyst beyond the limit of thermal resistance, resulting in deactivation of the catalyst. Further, this poses a danger, for example, that the residual hydrocarbon-type fuel in the apparatus may be mixed with the oxidant gas after the stopping of the apparatus. Thus, in stopping the operation, the present invention exerts such control as to decrease the flow rate of the hydrocarbon-type fuel and simultaneously increase the flow rate of water while maintaining the flow rate of the oxidant gas at a constant level, stop the hydrocarbon-type fuel, and thereafter stop the water and the oxidant gas.
Abstract:
A chemical reactor for catalytically processing a fluid feed stream comprises a reactor vessel incorporating a structured catalyst bed, and additionally comprises one or more catalytically active, fluid-permeable seals provided in gaps between the catalyst bed and the walls of the reactor vessel to treat portions of the fluid feed stream otherwise by-passing the structured catalyst for treatment.
Abstract:
The device is arranged in a process engineering column (10) and serves in particular for the guiding of liquid. This device includes at least two parts (1, 2) made of sheet metal and releasably connected to one another. A recess (12) is arranged in the one part, the sheet metal part (1) of a first kind, and an elevation (21) fitting into the recess is arranged in the other part, the sheet metal part (2) of a second kind. The two sheet metal parts are held in a secured position by a hook connection between the recess and the elevation. The recess and the elevation form a single pair or one pair among several and the sheet metal parts have planar regions lying on top of one another in the neighbourhood (120, 210) of the pair or of each pair respectively.
Abstract:
Device for mixing and distributing a dense, generally liquid, fluid and a light, generally gaseous, fluid, placed in a reaction chamber upstream from a granular bed (70) or between two successive granular beds, the said device being characterized by a tubular system (50) for the introduction of dense fluid from outside the reactor, up to a level lower than the level of establishment of the interface between the dense fluid and the light fluid, situated above the plate and preferably more or less next to that of the plate (62). Application of this device to any type of gas/liquid reaction in a fixed bed in particular for hydrotreatment.
Abstract:
A hydrocarbon-containing feed, e.g. naphtha, is converted in a treatment plant (1), in particular a refinery or olefin plant, into desired olefins, e.g. ethylene and propylene. At least part of the fractions comprising relatively long-chain olefins, in particular olefins having at least four carbon atoms, obtained from the treatment plant (1) is passed to an olefin conversion stage (12). In the olefin conversion stage (12), for example, a catalytic reactor, in particular a fixed-bed reactor, at least part of the relatively long-chain olefins is converted into relatively shorter-chain olefins. To increase the yield of desired olefins, the olefin conversion stage (12) is preceded by a paraffin/olefin separation stage (23) wherein the feed stream is separated into a paraffin stream, e.g., a stream comprising butane and pentane, and an olefin stream, e.g,. a stream comprising butene and pentene, e.g., by extractive distillation. The paraffins obtained are recirculated to the treatment plant (1), e.g., to the cracking furnace (3) of the olefin plant, and the olefins are fed to the olefin conversion stage (12).
Abstract:
Hydrogen is produced in a compact methanol-steam reformer, which integrates an inner cylindrical heating chamber; and a reactant vaporizer and heating zone, and an outer Cu/ZnO/Al2O3 catalyst bed in concentric annuli around the heating chamber. Tubular, palladium-silver alloy membranes in the catalyst bed separate hydrogen from retentate gas, which is separately discharged from the apparatus through a manifold.
Abstract translation:氢气在紧凑的甲醇 - 蒸汽重整器中产生,其集成了内圆柱形加热室; 和反应物蒸发器和加热区,以及位于加热室周围的同心环境中的外部Cu / ZnO / Al 2 O 3催化剂床。 催化剂床中的管状钯 - 银合金膜将氢气与滞留气体分开,其通过歧管从设备单独排出。
Abstract:
A multilayered ceramic chemical reactor and method of making the chemical reactor for use in an integrated fuel reformer in the form of a chemical combustion heating reactor or a steam reforming reactor. The ceramic chemical reactor including a three-dimensional multilayer ceramic carrier structure defining a cavity having a cofired porous ceramic support layer formed therein. The porous ceramic support layer further includes an immobilized catalyst formed on a surface of the porous ceramic support layer or entrapped within a plurality of voids formed in the porous ceramic support layer. The immobilized catalyst providing for a chemical reaction which converts input chemical reactants into chemical products and by-products. The cavity further includes a fuel inlet, an air inlet, and an outlet. The fuel processor includes a monolithic three-dimensional multilayer ceramic carrier structure defining a fuel reforming reactor, having heat provided by the integrated chemical reactor.
Abstract:
Conventional hydrogen purification apparatuses cannot be used satisfactorily for applications in which much time is required for startup of the apparatus, and the apparatus is repeatedly started and stopped at frequent intervals because of complicated handling. In a hydrogen purification apparatus comprising at least a catalysis body 1 removing carbon monoxide from a reformed gas containing hydrogen, carbon monoxide and steam, the catalyst body 1 is constituted by a carrier comprised of a complex oxide in which at least one of Mo, W and Re is compounded with Zr, or comprised of an oxide of one of Mo, W, Re and Zr, and at least one of Pt, Pd, Rh and Ru carried on the surface of the carrier.