Ammonia (NH₃) is a promising carbon-free fuel for decarbonizing energy systems, but its use in practical combustion systems is hindered by low flame stability and NOₓ emissions. Burning NH₃ with hydrogen (H₂) has been proposed to improve stability in conventional combustion systems; however, NOₓ emissions may persist or worsen. Moderate or Intense Low-Oxygen Dilution (MILD) combustion offers a pathway to suppress NOₓ through distributed reaction zones and reduced peak temperatures. The aim of this study is to stabilize pure NH₃ and characterize it with the H₂ addition in a semi-industrial reverse-flow furnace under MILD conditions. The experiments demonstrated the stabilization of pure NH₃ under MILD conditions without reactive enhancers, resulting in negligible NOₓ emissions but significant NH₃ slip. The impact of H₂ addition was assessed by analyzing how the transition from MILD to flame influences emissions. A transition from MILD to a lifted flame occurred at ∼14 % H₂, marked by a sharp rise in NOₓ and a steep decline in NH₃ slip. An optimal trade-off was observed at 12 % H₂, where NH₃ slip decreased from 2626 to 1336 ppm, accompanied by only a 12 ppm increase in NO, while maintaining MILD conditions. Decreasing the furnace temperature extended MILD combustion to 20 % H₂, but compared to the 12 % H₂, it caused higher NH₃ slip and only a slight reduction in NO, highlighting a trade-off between temperature control and NH₃ decomposition. The experimental findings were analyzed from a chemical kinetic viewpoint using a chemical reactor network approach. The results showed that NO reduction at H2≤20 % was dominated by thermal DeNOx, while NO formation at H₂≤80 % primarily originated from fuel-bound nitrogen. These findings advance the understanding of NH₃-H₂ MILD combustion at realistic scales and provide insight into the design of low-emission ammonia-based systems.
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