Abstract:
Chemical processes proceeding during incomplete oxidation of heavy hydrocarbons in multiphase nonideal systems are modeled. A program is developed for calculating the composition of products of incomplete oxidation of hydrocarbons with the use of equilibrium and kinetic models with allowance for imperfection of the gas phase and solutions. The yield of the product was calculated by the equilibrium and kinetic models to optimize the yield of hydrogen during incomplete oxidation of eicosane (C$_{20}$H$_{42}$) in the presence of water in the supercritical domain of state of the system. The data calculated by the kinetic model are compared with experimental data.
Keywords:combustion, heavy hydrocarbons, equilibrium, kinetics, supercritical state, modeling.