This investigation measured the impact of the liquid starting medium o
n syngas (H-2+CO) conversion via the Fischer-Tropsch (F-T) synthesis i
n a 11 continuous stirred tank reactor (CSTR). The experiments were co
nducted with a low-wax producing iron catalyst, so that the liquid med
ium composition was unaltered by accumulation of product wax throughou
t the experiment. Our results show a greater deactivation rate for the
F-T reaction in heavier starting media (Polywax-655, Allied AC-1702,
and Mobil F-T product wax) versus the lighter medium (n-octacosane). T
he syngas (H-2+CO) conversions were approximately equal and steady for
the first five days in both light and heavy, commercially available w
ax media. However, the conversions dropped more rapidly in the heavier
wax media (from 85% to 60% in 12-13 days), but only modestly in the l
ight wax media (from 90% to 85% in 15 days). An even sharper deactivat
ion rate occurred with the heavy Mobil F-T wax (from 85% to 60% in six
days). For all experiments, the water gas shift (WGS) ratio in the ou
tlet gases dropped concurrently. One proposed explanation for this inc
reased deactivation in the heavier waxes is that heavier products are
being formed by secondary reactions. These products could build up ove
r time and restrict the diffusion of hydrocarbon products and water va
por out of the pores. The presence of higher partial pressures of wate
r vapor could irreversibly oxidize the catalyst. (C) 1997 Elsevier Sci
ence B.V.