Single and binary metal molybdates, supported on silica (80 wt% active
phase/20 wt% SiO2), having the formula AMoO(4), where A=Ni, Co, Mg, M
n, and/or Zn, and some ternary molybdates having the formula Ni0.45Co0
.45X0.066MoO4, where X=P, Bi, Fe, Cr, V, and Ce, were investigated for
the oxydehydrogenation of propane to propylene. The reaction is catal
ytic and is first order in propane disappearance, consistent with the
abstraction of a methylene hydrogen being the rate limiting step. Prop
ane conversion and yields of propylene produced vary greatly with the
choice of the A metal of the molybdate and the surface area of the cat
alyst. At 560 degrees C and atmospheric pressure, the highest propane
conversion and highest propylene yields are obtained with NiMoO4/SiO2
(16% at 27% conversion), closely followed by Ni0.5Co0.5MoO4/SiO2. The
molybdenum content of the compositions greatly influences the catalyti
c activity and useful product yields. The effect is largest for the Ni
-molybdate system whose optimum lies at stoichiometry. The optimum act
ivity of Co-molybdate lies at molybdenum lean compositions. Binary Ni-
Co-molybdates are less sensitive to molybdenum level, offering a conve
niently stable catalytic system for further mechanistic and technologi
cal optimization studies. Addition of redox elements V, Fe, Ce, and Cr
enhances the activity of the Ni-Co-molybdates, with Cr addition holdi
ng most promise by retaining high selectivity at enhanced conversions
and hence a possibility for desired lower process temperature operatio
n. Our studies suggest, that the Ni-Co molybdate system provides an al
ternate to V-based catalysts for the activation of light paraffins. Fu
turistically, it holds promise as the paraffin activating component of
a two component catalyst system for the direct conversion, in a singl
e reactor, of propane to acrylic acid or acrylonitrile, with the secon
d component being composed of one of the well known olefin converting,
multicomponent mixed metal molybdates. (C) 1997 Academic Press.