A reformer tube for producing synthesis gas by steam reforming of hydrocarbon-containing feed gases, in which a structured stream reforming catalyst is used, is proposed. According to the invention, a heat exchanger tube is arranged in the interior of the structured catalyst, with the feed gas stream flowing firstly through the structured catalyst and subsequently in countercurrent through the heat exchanger tube. This improves the heat exchange between the synthesis gas product stream and the structured catalyst and the feed gas stream flowing through it, especially in the radial direction.

A device for heat, mass, and chemical exchange and interaction between gases and liquids. Nozzles feed the gas at angles in different directions to form a gas-liquid mix, swirls, and/or foam above an array of such nozzles.

The invention relates to a column having: a shell, which is extended along a longitudinal axis and encloses an interior of the column, at least one mass transfer tray, which is extended along a column cross section, extending transversely to the longitudinal axis, of the column, and at least one liquid distributor, which is designed to feed the at least one mass transfer tray with a liquid phase. In accordance with the invention, the mass transfer tray has a plurality of runoff elements extending parallel to and at a distance from one another, more particularly in the form of angular profiles, which are each extended along the column cross section, where the runoff elements each have first and second runoff surfaces extended along the column cross section, and where the two runoff surfaces converge along the longitudinal axis in the direction of the liquid distributor and meet, and in so doing form an edge extended along the column cross section, and where the liquid distributor is designed to apply the liquid phase to the edges of the runoff elements, so that the liquid phase applied to the respective runoff element flows off from the respective runoff element via the runoff surfaces at both sides of the respective edge.

A packing has a plurality of sheet materials spaced and arranged in parallel, and liquid flows along the flat surface thereof in a standing use state. Each sheet material has at least one member group including a plurality of support members arranged such that the upper end of the uppermost support member corresponds to the upper end of the sheet material and the lower end of the lowermost support member corresponds to the lower end of the sheet material. Each support member has a pair of support walls parallel to the liquid flow direction and perpendicular to the sheet material surface, and a bridging part connecting the support walls. A sandwiching structure is formed that one sheet material is held by at least one support member attached thereto and at least one support member attached to an adjacent sheet material, and it extends linearly through the plurality of sheet materials.

A reactor for carrying out catalytic reactions. The reactor includes a reactor component optionally arranged on a central rod in a reactor tube. The reactor component can have fluid ducts for directing fluid flow through the reactor. The fluid ducts are effective for increasing heat transfer in the reactor. The reactor component can further have a washer attached to a top or bottom surface for directing fluid flow.

An apparatus includes an inlet, an outlet, and a sheet disposed proximate a heat transfer surface, wherein the sheet is oriented in a sheet plane that is displaced from a plane of the heat transfer surface by an angle of at least 10 degrees. The apparatus also includes a plurality of tabs attached to the sheet, the tabs lying in respective tab planes, wherein the tab planes and the sheet plane intersect forming respective intersections. The intersections of the tab planes and the sheet plane are substantially parallel. The intersections of the tab planes and the sheet plane are at an angle of less than 88 to the heat transfer surface, and the plurality of tabs collectively form channels directing a fluid passing from the inlet to the outlet to impinge the heat transfer surface.

A genre of media is presented for use with a reactor vessel and for the purpose of immobilizing small particles, often catalytic in nature. The media can include a number of ferromagnetic active wafers stacked together and separated by non-ferromagnetic separator portions, such that when in the presence of a magnetic field and magnetic-particle-containing fluid, at least some of the gaps between active wafers captures and suspends magnetic particles.

A packing element has components that form snap-lock connections with like packing elements used to form a contact assembly. The packing elements can be readily and easily assembled together using little force by connecting the packing elements with connectors in a snap-lock manner. The packing elements are retained by the snap-lock connectors in the contact assembly such that the packing elements cannot be separated without such force that the material forming at least one of components of the snap-lock connections or the packing element will fail to the extent that a contact assembly made using the packing elements would not be functional.

A pulsed column for liquid-liquid extraction, including a cylindrical tube of longitudinal axis (Z) and inside diameter (D.sub.0) and packing located inside the tube. The packing includes a rod extending along the longitudinal axis (Z) and a plurality of truncated discs secured and regularly distributed along the rod with a separation (E) and each extending in a transverse plane (P) perpendicular to said rod, each of the truncated discs having, as their perimeter in the transverse plane (P), two arcs of a circle of radius (R) connected by two identical parallel rectilinear edges spaced apart by a distance (D), any two of the adjacent truncated discs being oriented with respect to each other in the transverse plane (P) by a non-zero orientation angle ().

A chemical flow reactor comprising: a housing having an inlet and an outlet; at least one heat exchange pipe extending through the interior of the housing; a space defined between the interior surface of the housing and the outer surface of Gas Flow the at least one pipe, said space being in fluid communication with the inlet and the outlet; and a plurality of plates stacked within said space forming a stacked plate assembly between the inlet and the outlet, each plate comprising at least one hole through which the at least one pipe extends such that the at least one pipe extends through the stacked plate assembly. An active chemical, such as a catalyst, is disposed on each plate.