Low load noble metal catalyst for dilute nitric acid reduction, preparation and application
A precious metal catalyst and dilute nitric acid technology, applied in the field of dilute nitric acid catalysis, can solve the problems of limited nitric acid conversion, low nitric acid concentration, high catalyst cost, etc., and achieve the effects of reduced production cost, good stability and good adaptability
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Embodiment 1
[0023] Take 0.259g of potassium nitrate solid, add 5.5g of deionized water to make an impregnation solution for additives; then take 5g of activated carbon particles between 14 mesh and 20 mesh, impregnate for 4 hours in equal volume, then dry at 100°C for 12 hours, N 2 Calcined at 200°C for 3 hours under protection to obtain a 2wt% K / AC standby sample.
[0024] Take 1.6ml of palladium nitrate solution (Pd content 4.688mg / mL) and add deionized water until the total mass of the mixed solution is 5.5g, configure it as an active component impregnation solution, take the K / AC prepared above, and impregnate it in equal volume for 4h, then Dry at 100°C for 12h, N 2 Burn at 300° C. for 3 h under protection to obtain a Pd-K / AC catalyst. The loading of Pd is 0.15%, and the loading of K is 2%. Catalyst A is recorded.
Embodiment 2
[0026] Adopt the method of embodiment 1, change the sodium nitrate of 0.259 potassium nitrate into 0.370, the mass content of Na is 2%, other remains unchanged, obtains Pd-Na / AC catalyst, the load of Pd is 0.15%, the load of Na The amount is 2%, and it is recorded as catalyst B.
Embodiment 3
[0028] Adopt the method of embodiment 1, change the amount of palladium nitrate solution, others remain unchanged, get respectively 0.53mL and 2.7mL palladium nitrate solution (Pd content 4.688mg / mL), make the loading capacity of auxiliary agent K respectively all be 2 %, and the catalysts with noble metal negative Pd loadings of 0.05% and 0.25%, respectively, are designated as Catalyst C and Catalyst D.
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