Detonation of HMX has been simulated using a multi-reaction chain and species equationof-states. A reacting flow code capable of handling arbitrary number of reactions and species has been used. Computational results are compared to the results produced by a pressurebased single reaction model (AJEX) and a temperature-based single-reaction model. Results show that the multi-reaction approach is capable of producing detonation calculations comparable to the AJEX model calculations, demonstrating that the multi-reaction approach possesses the properties required for the detonation modeling, a prerequisite of deflagrationto-detonation transition modeling. I. INTRODUCTION HMX (High Melting Explosive, Her Majesty's Explosive, C 4 H 8 N 8 O 8) has been used in polymerbonded explosives (PBX) such as PBX-9404, PBX-9501, LX-10, and LX-20. Its detonation behavior of course has been extensively studied. Detonation calculations are routinely carried out with pressure-based reactive burn models such as Forest-Fire [1], AJEX [2], and SURF (Scaled Unified Reactive Front) [3]. They typically employ one reaction mechanism in which the reactant (solid unreacted HE) turns into the product mixture. Species composition of the product is not calculated. There also are single reaction models with temperature-based reaction rates in the Arrhenius form [4]. But these models have not been so widely used as the pressure-based models. The Jones-Wilkins-Lee (JWL) equation-of-state (EOS) has been widely used when these types of modeling approaches are employed. Use of the pressure-based detonation models, however, present difficulties in the modeling of high explosives (HE) in some situations. Burning characteristics can be significantly affected by the reaction history such as the evolution of temperature and species in the modeling of deflagration covering a wide range of the temperature. For consistent modeling, it is necessary to use a multi-reaction model with temperature-based reaction rates. Furthermore, accurate tracking of temperatures would require EOS with temperature-dependent specific heats. In short, in order to advance HE modeling, we need to have multi-reaction chains with temperature-based reaction rates and temperature-dependent specific heats. Note that a species can be a reactant in a reaction while a product in other reactions. Furthermore, when temperature history changes, species concentrations would also change. To account for these aspects, thermodynamic states of each species need to be evaluated with its own EOS, which can be combined to calculate the thermodynamic states of the mixture. In summary, an approach employing a multi-reaction chain, temperature-based reaction rates, and species EOS is necessary in advanced modeling of HE such as DDT (deflagration-to-detonation transition). However, this approach has not been used for detonation calculations, which is a prerequisite for DDT calculations. That is, detonation needs to be captured by this approach in order to perform DDT modeling using a single unified frame...