Abstract: A catalytic converter reactor having in-built catalytic converter modules, wherein the total flow impingement surface area provided by the catalytic converter elements fitted in the catalytic converter modules is larger than the flow impingement surface area of the catalytic converter reactor, the module impingement surface area being defined by the catalytic converter module surfaces facing the main flow direction, and the catalytic converter modules being positioned so that the waste gas flows through the catalytic converter elements contained therein in a direction different from the flow direction on the intake and exit sides.

Abstract: A honeycomb body of ceramic material for use in installations for cleaning and/or regenerating gases, comprising a prismatic body, which is penetrated by many rectilinear gas-flow channels parallel to one another, which discharge into both face ends of the honeycomb body, wherein the honeycomb body (1) has at least one tubular recess (5, 5?), which is oriented transversely to the direction of the flow channels (4).

Abstract: A process for producing a honeycomb body from a noncatalytically active ceramic material for thermal regenerators, comprising the steps of (a) providing a block-shaped monolithic honeycomb body created by extrusion that includes in its interior longitudinal channels; (b) applying a thermal pretreatment to the honeycomb body; (c) after step (b), coating or masking the outer walls of the honeycomb body with a glaze-repellent coating, coating all the longitudinal channels of the honeycomb body with a glaze, and then drying the honeycomb body; and (d) after step (c), performing a firing operation at a temperature typical for the glazed material.

Abstract: Process for purifying and/or regenerating gases, in which the gas to be treated is fed to at least one layer of adjacently arranged prismatic honeycomb bodies (1) made of a ceramic material, which honeycomb bodies are provided with a plurality of channels (1?) which are parallel to one another and terminate in the end faces of the honeycomb bodies and through which the gas to be treated flows. The honeycomb bodies (1) are arranged in the layer at a predetermined lateral distance therebetween, which is fixed by two spacers (2) applied at two adjoining honeycomb body side walls (1?).

Abstract: A process for producing a honeycomb body from a noncatalytically active ceramic material for thermal regenerators, comprising the steps of (a) providing a block-shaped monolithic honeycomb body created by extrusion that includes in its interior longitudinal channels; (b) applying a thermal pretreatment to the honeycomb body; (c) after step (b), coating or masking the outer walls of the honeycomb body with a glaze-repellent coating, coating all the longitudinal channels of the honeycomb body with a glaze, and then drying the honeycomb body; and (d) after step (c), performing a firing operation at a temperature typical for the glazed material.

Abstract: Catalyst composition represented by the general formula REVO/S wherein RE is at least one of the group of rare earth metals Y, Ce, Pr, Nd, Sm, Gd, Tb, Dy, Er and Yb in an amount of up to 6.0 wt.-%; V is vanadium in an amount of 0.2-2.5 wt.-%; O is oxygen in an amount of up to 3.5 wt.-%; and S is a support containing TiO2 in an amount of at least 70 wt.-%, with the rest being WO3 and optionally SiO2. This catalyst composition shows high removal efficiencies for NOx even after aging at 750° C.