Three-way catalystic performances of Pd catalyst supported on Ni-aluminate
was superior than those supported on other supports. Adsorption and reducti
on properties of Ni-aluminate were investigated. The surface Ni2+ sites in
Ni-aluminate were shown to act the adsorption sites of NO under both oxidat
ive and reductive conditions. Under reductive conditions, in particular the
Ni2+ sites cropped out abundantly resulting in a great increase in the qua
ntity of NO adsorption. Ni-aluminate had higher resistance to the reduction
with H-2, allowing to be reduced at 800 degreesC and, after the reduction,
Ni-aluminate nearly recovered its previous state through a reverse process
of re-oxidation. The reduction with H-2 was enhanced by the presence of su
pported Pd; Partial reduction occurred at about 400 degreesC, and the reduc
tion peaks on the high temperature region shifted by about 50 degreesC. As
confirmed from the activity test by using a model gas mixture (C3H6-NO-O-2)
, the Ni-aluminate supported Pd catalyst was more efficient in light-off ac
tivity and NOx conversion activity under both stoichiometric and rich atmos
phere than the Pd catalyst supported on gamma -Al2O3. Based on these result
s, the excellent catalytic activity of the Ni-aluminate supported Pd cataly
st is considered to show up through a mechanism in which the Ni-aluminate p
rovides the adsorption sites for NO and transfer the adsorbed NO species to
the catalytic reaction sites of Pd.