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Cement rotary kilns face critical challenges in balancing carbon monoxide ( πΆ π ) and nitrogen oxide ( π β’ π π₯ ) emissions. To rigorously investigate burner aerodynamics without the prohibitive computational costs of multiphase reactions, this research employs a phase-decoupling approach, modeling the clinker bed as a dynamic heat sink. A comprehensive 3D computational fluid dynamics (CFD) simulation of methane non-premixed combustion is developed for a 1 0 0 0 t p d industrial rotary kiln. The coupled effects of Β± 2 0 % variations in primary air (PA) momentum on flame morphology, macro-mixing dynamics, and pollutant kinetics are evaluated using the Realizable π β β model, probability density function (PDF) approach, discrete ordinates (DO) radiation, and extended Zeldovich mechanism. Results reveal that a + 2 0 % increase in PA momentum enhances shear-layer turbulence and establishes a robust internal recirculation zone (IRZ). This accelerated macro-mixing reduces the methane burnout length from 8 . 1 m to 7 . 2 m and suppresses mixing-limited exit πΆ π mass fractions from 2 . 9 9 % to 1 . 4 0 % . Crucially, the enhanced flow advection reduces species residence time within the high-temperature zone ( π > 1 8 0 0 K ). This βaerodynamic quenchingβ mechanism restricts the slow Zeldovich kinetics, substantially decreasing the peak π β’ π π₯ mass fraction from 3 . 5 Γ 1 0 β 3 to 2 . 2 Γ 1 0 β 3 . Conversely, a 2 0 % momentum reduction weakens localized mixing, elevating both π β’ π π₯ and πΆ π ( 4 . 7 8 % ) emissions. Despite the simultaneous emission reduction benefits in the high-momentum scenario, it concentrates severe convective and radiative heat fluxes onto the refractory lining ( 5 β 1 1 m ), jeopardizing structural integrity. Ultimately, the baseline condition offers the most viable thermodynamic balance, demonstrating that tailored staged combustion is required to safely break the π β’ π π₯ - πΆ π trade-off.
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Nasiri et al. (2026) studied this question.
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