Oxygen-enriched tail gas nitrogen oxide purifying catalyst
A catalyst and tail gas technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, chemical/physical process, etc., can solve the problem of poor selectivity of noble metal catalysts, loss of reduced nitrogen oxides, poisoning, etc. question
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Embodiment 1
[0015] 100 grams of gamma-alumina powder (particle size less than 120 mesh, specific surface area: not less than 250 square meters per gram) is soaked in the mixed aqueous solution of silver nitrate, platinum chloric acid and ferric nitrate at a predetermined concentration, stirred for 1 hour, After drying at 90°C, raise the temperature from 100°C to 700°C step by step in the air, keep it for 3 hours, and then cool it down to room temperature. After crushing, take 0.5-1.0mm particles for later use as catalyst A. The silver component load of the finished product catalyst is 5.0% (metal element weight conversion value), the platinum component load is 0.25% (metal element weight conversion value), and the iron component load is 15.0% (metal element weight conversion value). value).
Embodiment 2
[0019] 1.5 grams of implementation catalyst A and comparison catalyst A made by the above method are placed in the tubular reactor respectively, and 4 liters / min of simulated lean combustion tail gas as shown in table 1 are introduced, corresponding to space velocity (GHSV) 50,000 / hour. The temperature of the simulated tail gas entering the reactor was raised from 200°C to 600°C, and the reduction of nitrogen oxides by propylene was observed when the catalytic reaction reached a steady state.
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