“…Due to its unique nature, SO 3 is difficult to remove effectively in widely used wet flue gas desulfurization (WFGD) systems. , Recently, dry-sorbent injection technology has become a promising method for SO 3 emission control. , The sorbent could be injected before the air preheater, at the economizer outlet or the SCR outlet, and then all SO 3 formed in the boiler furnace and SCR can be reduced . The SO 3 removal characteristics is mainly influenced by sorbent properties, flue gas parameters, reactor structure parameters, etc. , Different sorbents have been studied to absorb SO 3 in the literature, which are mainly sodium-, calcium-, and magnesium-based substance, such as NaHCO 3 , Na 2 CO 3 , Na 2 SO 3 , Ca(OH) 2 , ,− ,,, CaCO 3 , and Mg(OH) 2 . , Meanwhile, some researches focused on metal oxides, − like CaO, MgO, Na 2 O, and K 2 O, which are fly ash components, especially CaO, ,,, which is one of the main components of fly ash. For the wide industrial applications of dry-sorbent injection technology, selecting a suitable adsorbent material is of great importance .…”