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This study investigates the effects of fly ash compositions (SiO 2 and Al 2 O 3 ), particle sizes (4–10μm and 40μm), and concentrations on the simultaneous removals of fly ash and NO using a fluidized-bed catalyst reactor. Experimental results show that the removal efficiencies of fly ash and NO at particle concentrations of 968–11,181mgm −3 are 71–97% and 42–57%, respectively...
It is expected that the simultaneous removal of acid gases and particles from flue gas, using a single process and at the same temperature, will become an economical, and thus, desirable option. Accordingly, this study investigates the potential for the utilization of a fluidized-bed adsorbent/catalyst reactor for the simultaneous removal of SO 2 and fly ash from simulated flue gas. The operating...
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