The effects of NO
X
and O2 on the reaction of Ca(OH)2 with CO2 were studied
under low-temperature and humid conditions prevailing in dry or semidry
flue gas desulfurization processes. Without the simultaneous presence
of NO
X
and O2, the extent of
the carbonation of Ca(OH)2 was low and not affected by
the concentration of CO2, NO
X
, or O2. With the simultaneous presence of NO
X
and O2, the carbonation of Ca(OH)2 was greatly enhanced, and the CO2 capture increased
by more than 2 times at a relative humidity higher than 40%; in addition,
the relative humidity and NO
X
concentration
had positive effects, the temperature and O2 concentration
had negligible effects, but the CO2 concentration had a
negative effect. The simultaneous presence of NO
X
and O2 enhanced the formation of nitric and
nitrous acids and salts of calcium nitrate and nitrite. The deliquescence
of these salts collected a great quantity of water and thus enhanced
the reactions of Ca(OH)2 with the reactive gases. Ca(OH)2 could be completely converted when reacted with the mixture
of CO2, NO
X
, and O2 at a relative humidity ≥ 50% and a NO
X
concentration ≥ 300 ppm; CaCO3 formed
would further react with NO
X
and O2 to form Ca(NO3)2 when Ca(OH)2 was depleted. The highest CO2 capture obtained was 0.49
g of CO2/g of sorbent (reacted at 60 °C, 70% relative
humidity (RH), 12.6% CO2, 2400 ppm NO
X
, and 5% O2 for 1 h). The major products for
the reactions of NO2 with Ca(OH)2 and CaCO3 were calcium nitrite and nitrate, respectively. The capture
of CO2 in practice is preferably carried out before removing
NO
X
and after removing SO2 from
the flue gas. This work is useful to the development of technologies
for CO2 capture using solid wastes containing CaO/Ca(OH)2.