This paper presents a semidetailed kinetic scheme for the oxidation of
iso-octane (2,2,4-trimethyl-pentane). Both the low- and high-temperat
ure primary mechanisms are reduced to a lumped kinetic model involving
only a limited number of intermediate steps. This primary reaction sc
heme, similar to the one already presented for n-heptane [1], is flexi
ble enough to maintain accurate prediction of intermediate components,
heat release, and ignition delay times for a wide range of operating
parameter;. General criteria for the reduction of intermediate species
allow an efficient coupling with a detailed kinetic model of C-1-C-4
oxidation. Thermochemical oscillations and the negative temperature co
efficient (NTC) region of the reaction rate of the low-temperature oxi
dation of iso-octane in a jet-stirred reactor are reproduced quite wel
l by the model. Several comparisons with experimental data, obtained u
nder very different operating conditions, including a shock tube, a ra
pid compression machine, dow and jet-stirred reactors, support the app
licability of this model of iso-octane oxidation over a wide range of
pressures, temperatures, and mixture compositions. Copyright (C) 1997
by The Combustion Institute