The removal of nonconventional
pollutants in coal-fired power plants,
such as SO3, has been receiving more and more attention.
However, due to its unique nature, it is difficult to remove SO3 effectively with the widely used wet flue gas desulfurization
systems. Nowadays, dry-sorbent injection technology has become a promising
method for SO3 emission control in coal-fired power plants.
The removal characteristics of SO3 from flue gas with modified
fly ash adsorbents were investigated in a fixed-bed reactor. Factors
affecting the adsorption efficiency of SO3 were studied,
including modification method, modified fly ash adsorbent particle
size, reaction temperature, and flue gas component. Combined with
adsorbent characterization analysis, the adsorption kinetics of SO3 by modified fly ash adsorbents were carried out with four
different adsorption kinetics models. The results show that the SO3 adsorption efficiency of the fly ash samples increases after
modification; the best SO3 removal performance of fly ash
was achieved when 1.5 mol/L NaOH solution was used, with the highest
SO3 adsorption efficiency of up to 98.3%. The modified
fly ash adsorbent particle size, water vapor content, and the addition
of NO have little effect on the adsorption efficiency of SO3. As the reaction temperature increases from 250 to 450 °C,
the SO3 adsorption efficiency first increases and then
decreases, with an optimal reaction temperature of 350 °C. The
addition of SO2 would compete with SO3 for adsorption
and inhibit the uptake of SO3 by the adsorbent. Adsorption
kinetics data show that external mass transfer and chemical adsorption
are the main critical mechanisms affecting the adsorption efficiency
of the modified fly ash adsorbent in the SO3 removal process
compared to internal diffusion.