Abstract: A metallic catalyst carrier body for the cleaning or treatment of an exhaust-gas flow, in particular of small engines, includes a multiplicity of strip-shaped foils which are joined together in the form of a honeycomb structure. The foils form a foil assembly structure in which mutually adjacent respective foils are securely interconnected at connecting locations that are spaced apart from one another and offset alternatingly relative to one another. If the foil assembly is stretched, for example by winding the same into a hollow body, the honeycomb structure is formed, defining flow channels with at least one radial directional component in its interior, through the use of cells.

Abstract: A Fischer-Tropsch catalyst for the conversion of synthesis gas into Fischer-Tropsch products includes a stationary Fischer-Tropsch catalyst having a voidage ratio greater than approximately 0.45 or 0.6 and may further have a catalyst concentration for a given reactor volume of at least 10 percent. A Fischer-Tropsch catalyst has a structured shape promoting non-Taylor flow and/or producing a productivity in the range of 200-4000 vol CO/vol. Catalyst/hour or greater over at least a 600 hour run of a Fischer-Tropsch reactor with the catalyst therein. A system for converting synthesis gas into longer-chain hydrocarbon products through the Fisher-Tropsch reaction has a reactor for receiving synthesis gas directly or as a saturated hydrocarbon liquid or a combination, and a stationary, structured Fischer-Tropsch catalyst disposed within the reactor for converting at least a portion of the synthesis gas into longer-chain hydrocarbons through Fischer-Tropsch reaction.

Abstract: A ceramic filter module includes a plurality of passage holes (11) and internal passage holes (12) alternately arranged about a plurality of ceramic partitions (15). The internal passage holes are sealed at each end by seals (13). The partitions are at most 1 mm thick and allow fluid to be filtered as the fluid flows from passage holes (11) to the internal passage holes (12). A plurality of discharge holes (14) traversing through the ceramic partitions between adjacent internal passage holes or between an internal passage hole and an outer surface allow the permeate to exit. The module is a porous ceramic body that preferably has an average pore diameter of 1 &mgr;m and is composed of silicon nitride. The ceramic filter module has the advantages of low permeation resistance and very high permeability.