An
iron-based catalyst with excellent performance and low price
was used for simultaneous removal of SO2 and NO
x
in a typical Fenton system. The catalyst was developed
from fly ash of pulverized coal furnace by alkali-magnetic modification
process. In other words, the raw fly ash was first modified by Ca(OH)2, which destroyed the vitreous shell and made the internal
substances such as Al2O3, SiO2, and
Fe2O3 dissolve out gradually, and then separated
magnetically and roasted, and the high magnetic Fe2O3 content of high reactivity was obtained. In the fixed bed
experimental system, an ultrasonic nebulizer was adopted to atomize
hydrogen peroxide which can reduce the particle size of hydrogen peroxide
and shorten the gasification time greatly. Effects of the concentration
of hydrogen peroxide, reaction temperature, iron oxide content, and
initial concentration of SO2 and NO
x
on the collaborative removal efficiencies were investigated.
Under low hydrogen peroxide concentration (1 mol/L) and flow rate
(0.03 mL/min), 100% desulfurization efficiency and 90% denitrification
efficiency can be achieved using hydrogen peroxide catalyzed by the
modified fly ash. The catalytic mechanism and reaction mechanism were
analyzed by XRF, XRD, ESR, SEM, BET, and XPS.