A treatment process was developed when basic oxygen furnace slag (BOF slag)
and hydrogen peroxide were used to oxidize 2,4-dinitrophenol from an aqueo
us solution. BOF slag, final waste slurry from steel making plants, contain
s about 12.5% by weight of ferrous oxide. In an acid solution, BOF slag can
be dissociated to produce ferrous ions and react with hydrogen peroxide to
produce hydroxyl radicals and oxidize 2,4-dinitrophenol. The results of th
e research demonstrated that the process had a significant capacity for oxi
dation of 2,4-dinitrophenol from the aqueous phase. Various factors critica
l to the oxidation of 2,4-dinitrophenol were studied, including hydrogen pe
roxide concentration, concentration of BOF slag, initial concentration of 2
,4-dinitrophenol, and pH value of solution. Experimental results proved tha
t 100 mg/L 2,4-dinitrophenol and its oxidation intermediate could be totall
y decomposed within 60 min by 10 g/L BOF slag, 0.18 g/L hydrogen peroxide a
nd pH 2.8 +/- 0.2. The optimum hydrogen peroxide concentration for degradat
ion of 100 mg/L of 2,4-dinitrophenol is between 0.09 g/L and 0.18 gn as 10
g/L BOF slag in the solution of pH 2.8 +/- 0.2. A hydrogen peroxide concent
ration higher than 0.18 g/L is disadvantageous to the oxidation process. Th
e oxidation efficiency increased with the increase of BOF slag concentratio
n at 0.18 g/L hydrogen peroxide dose. The best pH value of the solution is
in the vicinity of 2.8. An oxidation reaction mechanism was proposed for pr
edicting the concentration changes of 2,4-dinitrophenol, ferrous ion, and h
ydrogen peroxide.