This work evaluates the simultaneous removal efficiency of NO (1000 ppm) and SO
2 (1550 ppm) from flue gas induced by the combined temperature and Fe
2+ (0.01M) activation of aqueous persulfate (0.1M) and elucidates the chemistry and reaction pathways. The results indicated that both SO
2 in the flue gas and Fe
2+ in solution improved NO removal. The conversion of NO (i.e., percent removal of inlet concentration) was 46.2% at 30°C and only slightly to 48.2% at 50°C; but sharply increased to 81.2% at 70°C, while SO
2 was completely removed at all temperatures. Also, a kinetic-mass transfer mathematical model utilizing the pseudo-steady state approximation technique for proposed comprehensive reaction pathways was developed. The model results, which appeared to fit the experimental results of the NO
x-S(IV)-S
2O
82--Fe
2+ system remarkably well, was used to predict species and product concentrations, NO and SO
2 mass transfer coefficients, kinetic data and other process parameters.
References:
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