The commercially available V2O5/WO3–TiO2 is a well-known
catalyst for selective catalytic
reduction (SCR) of NO with NH3. When alkali ions are present
in the exhaust (e.g., as impurities such as dust) of a reactor containing
commercial V2O5/WO3–TiO2, alkali poisoning occurs, deactivating the catalyst. Consequently,
there is substantial interest in the development of better-performing
and more durable NH3–SCR catalysts with an improved
resistance to alkali deactivation. For the present study, the protonated
(H+) form of zeolite Y, HY, was used as a support and acted
as buffer zone, leading to trapping (sticking) of foreign alkali poisons
in the zeolite pore structure, preventing alkali poisoning of the
Fe2O3/HY catalyst. Catalytic tests showed that
the Fe2O3/HY retained 100% of its original catalytic
reactivity for NH3–SCR reaction even after 1000
μmol Na+ g–1 poisoning. 1000 μmol
Na+ g–1 treatment indicates a 26 000-h
exposure under an alkaline dust-containing condition. In contrast,
upon 1000 μmol Na+ g–1 treatment,
severe alkali deactivation occurred for a commercial V2O5/WO3–TiO2. The catalyst
activity of Fe2O3/HY remained unchanged because
of the intercalation of Na+ in the internal HY zeolite
pores that impedes the blocking of Na+ poison to the external
active sites of Fe2O3. The findings in this
work suggest that the zeolite HY may be revealed as an attractive
building block for designing an alkali poisoning-resistant catalyst.