Ammonia's slow chemical kinetics and fuel-bound NOx emissions present challenges for combustion applications. However, its carbon-free nature, easy storage and transport, and high hydrogen content have attracted growing research interest. To improve the burning efficiency of pure ammonia flames, this study introduces a novel burner design with two reactor sets, aimed at achieving stable ammonia-air flames with reduced NOx zero NH3 slip. Experiments are conducted and successfully stabilised the pure ammonia flames under the wide range of global equvalence ratios (0.3-1.3) and thermal intensities (∼1.5 MW/m3 to ∼9.2 MW/m3). Emissions of NH3, NO, and NO2, along with temperatures at various combustor levels, are measured. Computational simulations using Large Eddy Simulation (LES) are conducted to study flame dynamics and mixing in pure ammonia flames. The results indicated that the new burner design enhanced flame stability (0.3-1.3), improved mixing, achieved nearly zero NH3 slip, and reduced NOx levels in non-premixed ammonia-air flames. Both experimental and predicted data revealed that higher thermal intensities are key to reducing NH3 and NOx emissions across all equivalence ratios. At lower thermal outputs (10 kW and 20 kW), minimal NH3 emissions were noted at rich conditions (1.3), while higher thermal outputs completely eliminated NH3 emissions. The burner's air staging and recuperative design resulted in lower NO emissions compared to previous studies, with the lowest NO levels (420, 302, 390, and 299 ppm) at 10, 20, 40, and 60 kW, respectively, without NH3 emissions. Rich conditions produced well-distributed flames at 40 kW and 60 kW. A chemical reaction network (CRN) analysis showed the influence of O2 availability and thermal intensities on NO emissions, confirming that uniform mixing from tangential air inlets effectively controlled ammonia consumption.
Investigation of the pure ammonia flames in a novel two-stage burner
Sorrentino G.;de Joannon M.;
2025
Abstract
Ammonia's slow chemical kinetics and fuel-bound NOx emissions present challenges for combustion applications. However, its carbon-free nature, easy storage and transport, and high hydrogen content have attracted growing research interest. To improve the burning efficiency of pure ammonia flames, this study introduces a novel burner design with two reactor sets, aimed at achieving stable ammonia-air flames with reduced NOx zero NH3 slip. Experiments are conducted and successfully stabilised the pure ammonia flames under the wide range of global equvalence ratios (0.3-1.3) and thermal intensities (∼1.5 MW/m3 to ∼9.2 MW/m3). Emissions of NH3, NO, and NO2, along with temperatures at various combustor levels, are measured. Computational simulations using Large Eddy Simulation (LES) are conducted to study flame dynamics and mixing in pure ammonia flames. The results indicated that the new burner design enhanced flame stability (0.3-1.3), improved mixing, achieved nearly zero NH3 slip, and reduced NOx levels in non-premixed ammonia-air flames. Both experimental and predicted data revealed that higher thermal intensities are key to reducing NH3 and NOx emissions across all equivalence ratios. At lower thermal outputs (10 kW and 20 kW), minimal NH3 emissions were noted at rich conditions (1.3), while higher thermal outputs completely eliminated NH3 emissions. The burner's air staging and recuperative design resulted in lower NO emissions compared to previous studies, with the lowest NO levels (420, 302, 390, and 299 ppm) at 10, 20, 40, and 60 kW, respectively, without NH3 emissions. Rich conditions produced well-distributed flames at 40 kW and 60 kW. A chemical reaction network (CRN) analysis showed the influence of O2 availability and thermal intensities on NO emissions, confirming that uniform mixing from tangential air inlets effectively controlled ammonia consumption.| File | Dimensione | Formato | |
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