Terminally oxidized hydrocarbons are of considerable interest as potential
feedstocks for the chemical and pharmaceutical industry, but the selective
oxidation of only the terminal methyl groups in alkanes remains a challengi
ng task. It is accomplished with high efficiency and selectivity by some en
zymes; but inorganic catalysts, although inferior in overall performance un
der benign conditions, offer significant advantages from a processing stand
point(1). Controlled partial oxidation is easier to achieve with 'sacrifici
al' oxidants, such as hydrogen peroxide(2), alkyl hydroperoxides or iodosyl
benzene(3), than with molecular oxygen or air. These sacrificial oxidants,
themselves the product of oxidation reactions, have been used in catalytic
systems involving: tailored transition-metal complexes in either a homogene
ous state(4-6), encapsulated in molecular sieves(7-9) or anchored to the in
ner surfaces of porous siliceous supports(10). Here we report the design an
d performance of two aluminophosphate molecular sieves containing isolated,
four-coordinated Co(III) or Mn(III) ions that are substituted into the fra
mework and act, in concert with the surrounding framework structure, as reg
ioselective catalysts for the oxidation of linear alkanes by molecular oxyg
en. The catalysts operate at temperatures between 373 K and 403 K through a
classical free-radical chain-autoxidation mechanism. They are thus able to
use molecular oxygen as oxidant, which, in combination with their good ove
rall performance, raises the prospect of using this type of selective inorg
anic catalyst for industrial oxidation processes.