The kinetics of n-hexane oxyfunctionalization over a series of titaniu
m silicalites (TS-1) has been investigated using aqueous hydrogen pero
xide (30 wt %). The oxyfunctionalization reaction has been modeled usi
ng results from a batch reactor. All catalysts were also characterized
using analytical techniques such as XRD, UV-vis, and FT IR spectrosco
pies. The intrinsic kinetic constants were found to be proportional to
the fraction of T atoms substituted with titanium in the TS-1 framewo
rk. This kinetic analysis indicates a substitutional limit of 1.9% T a
toms, in full agreement with previous literature data obtained by anal
ytical techniques. The effects of temperature and extra-framework tita
nium are also discussed.