Process for decreasing the content of nitrogen oxides in flue gases
AssigneeSud-Chemie AG
InventorsMichael Schneider, Hans J. Wernicke, Karl Kochloefl, Gerd Maletz
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AssigneeSud-Chemie AG
InventorsMichael Schneider, Hans J. Wernicke, Karl Kochloefl, Gerd Maletz
Estimating the term…
A process for decreasing the content of nitrogen oxides in flue gases. The process comprising contacting the flue gases with a catalyst. The catalyst contains at least one of the metals titanium, zirconium, vanadium, tungsten, molybdenum, or cerium in the form of one or more of their oxides combined with a silicate with a layer structure (layer silicate) comprising acid-activated kaolin. The crystalline layer structure of the acid-activated kaolin is essentially retained, while being not yet X-ray amorphous. The acid activation increases the BET surface area at least 15% and preferably at least 50% in terms of the BET surface area of the kaolin before acid activation. The atomic ratio of the silicon in the acid-activated kaolin to the metal in the oxide is from 0.2 and 50 and preferably from 0.4 to 25.
A process for reductively decreasing the content of nitrogen oxide in flue gases that contain sulfur oxides, the process comprising contacting the flue gases with a catalyst and with NH.sub.3, which is employed as a reductant, said catalyst comprising at least one metal selected from the group consisting of titanium, zirconium, vanadium, tungsten, molybdenum and cerium in the form of one or more of their oxides and a silicate with a layer structure comprising acid-activated, but not yet X-ray amorphous kaolin whose crystalline layer structure is partly retained, the acid activation increasing the BET surface area at least 15% in terms of the BET surface area of the kaolin before acid activation, and the atomic ratio of the silicon in the acid-activated kaolin to the metal in the oxide being between 0.2 to 50, wherein the process is conducted at a temperature of 350.degree. C. to 600.degree. C., wherein the metal in the catalyst is present in an amount of 0.1 to 80% by weight, with the acid-activated kaolin accounting for the rest of the catalyst weight.
Dependencies are inferred from the claim text.