Abstract
The oxidation of ammonia-dimethoxymethane (NH(3)-DMM) mixtures at high pressure was analyzed from both experimental and kinetic modeling points of view. Experiments were performed using a laboratory tubular flow reactor installation and were conducted at 10, 20, and 40 bar under fuel-rich (λ = 0.7), stoichiometric (λ = 1), and fuel-lean (λ = 3) conditions and temperatures ranging from 650 to 1250 K. The inlet DMM concentration was varied (100 and 200 ppm), keeping the concentration of ammonia constant at 1000 ppm. The data were interpreted in terms of a detailed chemical kinetic model. Despite some discrepancy between the model predictions and measurements, the model accurately followed the experimental trends, highlighting its ability to describe the oxidation of the NH(3)-DMM mixture. The experimental and predicted results suggested that the conversion of both ammonia and DMM was favored by increased pressure and higher inlet concentrations of O(2) and DMM. Under the conditions of the present work, the dominant path for ammonia and DMM conversion leads to N(2)/N(2)O and CO/CO(2) in any case. Concentrations of NO and NO(2) were below the detection limit in all the experimental conditions studied, which imply a benefit in the reduction of NO (x) emissions during the combustion of pure ammonia. DMM enhanced the ammonia reactivity, although its presence leads to the formation of CO(2) not only by the common CO + OH reaction but also through the interaction of N(2)O with CO.