Liquid-phase air oxidation of hydrocarbons, notably p-xylene, cumene, ethylbenzene/isobutane,
cyclohexane, and n-butane, is of great scientific, technological, and commercial importance. This
state-of-the-art paper covers the chemistry and engineering science aspects of these reactions.
The role of uncatalyzed reactions and metal ion and mixed metal ion catalysts with bromide
activation is discussed. An analysis is presented for the role of mass transfer in influencing the
rate of reaction and selectivity for the desired product. Different types of reactors that are used,
notably bubble-column reactors and mechanically agitated reactors, are analyzed, and a simple
basis is provided for selection of reactors. Some emerging oxidation systems, notably oxidation
of cycloalkenes (cyclohexene/cyclooctene/cyclododecene) and oxidation of isobutane under supercritical conditions, are presented. New strategies for conducting air oxidations, such as in
biphasic systems (including fluorous biphasic systems), biocatalysis, photocatalysis, etc., are
emerging and illustrate the considerable tailoring of the reaction microenvironment that is
becoming possible. In some cases, it may be possible to manipulate chemo-, regio-, and enantioselectivity in these reactions.