Vanadium-free catalyst for selective catalytic reduction and process for its preparation
A catalyst and reducing agent technology, applied in the field of catalysts, can solve problems such as difficult preparation, unsatisfactory use in motor vehicle activity and aging stability, and achieve cost-effective results
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Embodiment 1
[0075] A center sample was taken from the catalyst of Comparative Example 1 and sulfided in a furnace at 350°C for 48 hours in an atmosphere of 10 vol% oxygen, 10 vol% water, and 20 vol-ppm sulfur dioxide in nitrogen. The catalyst K1 obtained according to the invention was studied in a model gas.
[0076] figure 2 Shown are the nitrogen oxide conversions of catalyst K1 (●) according to the invention compared to comparative catalysts VK3 (◇, iron-zeolite-based), VK4 (□, vanadium-containing) and VK5 (×, Fe / W / ZrO 2 ) conversion rate of nitrogen oxides. Catalyst K1 according to the invention exhibits a higher conversion of nitrogen oxides in the SCR reaction over the entire temperature range than the comparative catalyst VK5 according to the prior art (which is also zeolite- and vanadium-free). Also surprisingly, in the temperature range from 300°C to 500°C, the nitrogen oxide conversion performance of the commercially available iron-zeolite-based catalyst VK3 was exceeded and...
Embodiment 2
[0078] A center sample was taken from the catalyst of Comparative Example 2 and sulfided in a furnace at 350°C for 48 hours in an atmosphere of 10 vol% oxygen, 10 vol% water, and 20 vol-ppm sulfur dioxide in nitrogen. The catalyst K2 obtained according to the invention was studied in a model gas.
[0079] image 3 The results of this study are shown and compared with the existing SCR catalysts VK3 (◇, based on iron-zeolite), VK4 (□, containing vanadium) and VK5 (×, Fe / W / ZrO 2 ) conversion rate of nitrogen oxides. The catalyst K2 according to the invention also exceeds the conversion performance of VK5 over the entire temperature range and the nitrogen oxide conversion performance of the iron-zeolite-based catalyst VK3 at temperatures above 300° C. The nitrogen oxide conversion performance of the vanadium-based comparative catalyst VK4 is fully achieved from 350° C. onwards.
Embodiment 3
[0081] A homogeneous cerium-zirconium mixed oxide with a ceria content of 48% by weight, based on its total amount, was activated for the SCR reaction by introducing tungsten. For this purpose, the amount of water which the homogeneous cerium-zirconium mixed oxide could absorb was first measured without the material losing its free-flowing properties. A tungsten compound having good water solubility in a proportion corresponding to 10% by weight of tungsten, based on the total weight of the activated cerium-zirconium mixed oxide to be produced, was dissolved in the corresponding amount of water. The tungsten-containing solution thus prepared was impregnated with the homogeneous cerium-zirconium mixed oxide until the pores were filled, and then stored in air in a furnace at 500° C. for 2 hours for thermal curing of the tungsten.
[0082] The activated cerium-zirconium mixed oxide thus obtained was suspended in water, ground and applied to a ceramic honeycomb element with a volu...
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