The NO, NO/O-2, and NO/O-2/H2O adsorption on MnO2/NaY (5 and 15 wt.% MnO2)
composite catalyst and NaY has been studied by means of in situ FTIR and EP
R spectroscopy at elevated temperatures and during heating under reaction-l
ike conditions. NO adsorption and co-adsorption of NO and O-2 on NaY and Mn
O2/NaY proceeds via oxidation of NO forming NO2- and NO3- species. Whereas
the manganese dioxide preferably acts as oxidising agent, the zeolite store
s the NOx species as nitrite and nitrate ions in the solid. In the presence
of oxygen, the nitrate formation is enhanced due to additional oxidation o
f NO through gaseous oxygen leading to NO2. Dimerisation of NO2 to N2O4 and
following disproportionation of the latter causes the formation of NO+ and
NO3- species which are associated with nucleophilic zeolitic oxygen and es
pecially alkali cations of the zeolite, respectively. The presence of oxyge
n facilitates reoxidation of Mn2+ which keeps more Mn ions in the active st
ate. Pre-adsorbed water and higher amounts of water vapour in the feed hind
er the NO adsorption by blocking the adsorption sites and shift the nitrate
formation to higher temperatures. The quantities and thermal stability of
the nitrates formed during NO and NO/O-2 adsorption differs which points to
a different mechanism of nitrate formation. In the absence of gaseous oxyg
en, nitrates are formed by participation of only lattice oxygen. In the pre
sence of oxygen, nitrate formation by dimerisation and disproportionation r
eactions of NO2 dominates. The manganese component of the composite catalys
t supports the oxidation of NO to nitrite and subsequently to nitrate. Duri
ng this process Mn4+ is reduced to Mn2+ as evidenced by in situ EPR measure
ments. (C) 2001 Elsevier Science B.V All rights reserved.