Abstract
A systematic comparison was made of the catalytic activity of a variety of Fe/zeolite catalysts in the selective catalytic reduction of NOx with iso-butane or propane, both with dry and wet feeds. All catalysts were prepared by subliming FeCl3 vapor onto the H-form of the zeolite, followed by Cl removal. The activities decrease in the order Fe/BEA > Fe/MFI ≫ Fe/FER > Fe/MOR ≈ Fe/Y. These differences are rationalized in terms of our mechanistic model and the known pore geometry of the zeolites. FT-IR shows that some Fe loaded narrow pore zeolites are able to oxidize NO to NO2 and form NOy chemisorption complexes, but unable to let iso-butane enter the pores. Unlike some wider pore zeolites that become covered by a carbonaceous deposit at low temperature, these materials retain their high activity for NO oxidation. Mixtures of Fe loaded wide and narrow pore zeolites, therefore, lead to higher steady-state activities at low temperature than single catalysts. In particular, the combination of Fe/MFI with Fe/FER displays a spectacular activity enhancement.
Original language | English |
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Pages (from-to) | 159-168 |
Number of pages | 10 |
Journal | Applied Catalysis A: General |
Volume | 194 |
DOIs | |
State | Published - Mar 13 2000 |
Externally published | Yes |
Funding
Financial support from the Director of the Chemistry Division, Basic Energy Sciences, U.S. Department of Energy, Grant DE-FGO2-87ER13654, is gratefully acknowledged.
Funders | Funder number |
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U.S. Department of Energy | DE-FGO2-87ER13654 |
Basic Energy Sciences |