A detailed chemical kinetic model has been used to study dimethyl ethe
r (DME) oxidation over a wide range of conditions. Experimental result
s obtained in a jet-stirred reactor (JSR) at 1 and 10 atm, 0.2 less th
an or equal to phi less than or equal to 2.5, and 800 less than or equ
al to T less than or equal to 1300 K were modeled, in addition to thos
e generated in a shock tube at 13 and 40 bar, phi = 1.0 and 650 less t
han or equal to T 1300 K. The JSR results are particularly valuable as
they include concentration profiles of reactants, intermediates, and
products pertinent to the oxidation of DME. These data test the kineti
c model severely, as it must be able to predict the correct distributi
on and concentrations of intermediate and final products formed in the
oxidation process. Additionally, the shock-tube results are very usef
ul, as they were taken at low temperatures and at high pressures, and
thus undergo negative temperature dependence (NTC) behavior. This beha
vior is characteristic of the oxidation of saturated hydrocarbon fuels
, (e.g., the primary reference fuels, n-heptane and iso-octane) under
similar conditions. The numerical model consists of 78 chemical specie
s and 336 chemical reactions. The thermodynamic properties of unknown
species pertaining to DME oxidation were calculated using THERM. (C) 1
998 John Wiley & Sons, Inc.