The catalytic ammonia synthesis activities of four supported ruthenium cata
lysts are reported. It is seen that Ru/MgAl2O4 is more active than two simi
lar Ru/C catalysts, which are significantly more active than Ru/Si3N4. The
activity differences cannot be satisfactorily explained solely by the diffe
rences in dispersion. Recent results from single crystal studies and DFT ca
lculations have shown that ammonia synthesis over ruthenium catalysts is a
very structure sensitive reaction, more so than on iron catalysts. It is su
ggested that special Bs-type sites are primarily responsible for the cataly
tic activity of the present supported Ru catalysts. It is shown how the num
ber of such Bs-type sites depends on the Ru crystal size for a given crysta
l morphology. We have found that the activity of the Ru/MgAl2O4 catalyst in
creases significantly during the initial part of a test run. This activity
increase is paralleled by the disappearance of crystals smaller than ca. 1.
0nm due to sintering and a resulting formation of larger crystals. We concl
ude that there exists a lower limit to the desired crystal size of Ru in su
pported ammonia synthesis catalysts. This is in agreement with a low number
of Bs-type sites expected for such crystal sizes. Furthermore, we suggest
that the support plays a decisive role in controlling the morphology of the
Ru crystals and the resulting change in abundance of Bs-type sites is the
main cause for the significant activity variations observed for Ru catalyst
s with different supports. Finally, the support may also influence the elec
tronic and catalytic properties of neighboring Bs-type sites. (C) 2000 Else
vier Science B.V. All rights reserved.