Detailed thermal degradation mechanisms for in use distillate fuels are not available, since fuel composition is very complex and the resulting degradation products are many. This makes the study of multicomponent fuel degradation and associated reaction mechanism elucidation a very complex task. A basic approach for studying the thermal degradation problem is to understand the detailed behavior of a prototypical fuel component, i.e., a n-alkane, and then extend the study to include binary and ternary fuel component combinations, dopants, etc. This approach was undertaken to study a single-component model fuel, n-dodecane, and the results are reported here. The data from the present neat n-dodecane experiments agreed with Hazlett et al.'s pioneering work, thereby verifying both sets of data. Also, new products were detected and identified, leading to a modification of the existing n-dodecane/oxygen reaction mechanism. n-Dodecane was aerated by bubbling air through the hydrocarbon and then was stressed on a modified jet fuel thermal oxidation tester facility between 200 and 400 °C. Gas chromatography and mass spectrometry analysis of the control and stressed samples yielded reaction mechanism information. The soluble products consisted mainly of C6-C10 n-alkanes and 1-alkenes, C7-C10 aldehydes, tetrahydrofuran derivatives, dodecanol and dodecanone isomers, dodecyl hydroperoxide (ROOH) decomposition products, and C24 alkane isomers. The modified n-dodecane oxidation mechanism shows that alkyl peroxyl radical reactions dominate in the autoxidation temperature regime (T < 300 °C). The dominant path is for the alkyl peroxyl radical, R02', to react bimolecularly with fuel to yield primarily alkyl hydroperoxides. R02* also undergoes self-termination and unimolecular isomerization and decomposition reactions, to yield smaller amounts of C12 alcohol plus ketone products and tetrahydrofuran derivatives, respectively. Thus, alcohol and ketone formation in this temperature regime implies that the main termination step is via R02* self-termination reactions, which refutes an earlier hypothesis that R* radical termination reactions (giving CM hydrocarbon isomers) are important. In the intermediate temperature regime (300 < T < 400 °C), the alkyl radical, R', reactions dominate the R02* reactions. The dominant reaction steps include (i) alkyl hydroperoxide (ROOH) and surface-initiated fuel pyrolysis reactions yielding