2013
DOI: 10.1016/j.fuel.2012.07.050
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Studies on magnesium-based wet flue gas desulfurization process with oxidation inhibition of the byproduct

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Cited by 69 publications
(41 citation statements)
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“…Both the amounts of excessive lactic acid and the consumption of calcium salt are determined by the amount of CaSO 4 produced. Currently, there are mature technologies to inhibit the oxidation of sulfite salts, such as CaSO 3 , Na 2 SO 3 and MgSO 3 [5,6,[19][20][21]. For example, an oxidation ratio between 4% and 10% is usually designed in the limestone inhibited oxidation process (LSIO) [1].…”
Section: Comparison Of Cal 2 Methods With Other Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Both the amounts of excessive lactic acid and the consumption of calcium salt are determined by the amount of CaSO 4 produced. Currently, there are mature technologies to inhibit the oxidation of sulfite salts, such as CaSO 3 , Na 2 SO 3 and MgSO 3 [5,6,[19][20][21]. For example, an oxidation ratio between 4% and 10% is usually designed in the limestone inhibited oxidation process (LSIO) [1].…”
Section: Comparison Of Cal 2 Methods With Other Methodsmentioning
confidence: 99%
“…Therefore, regenerable technologies show many advantages for the capture of SO 2 . It is well known that sodium method [3,4], magnesium method [5,6] and amine method [7,8] have been commercially used in the process of desulfurization of flue gas. Besides the commercially used methods, the absorption of SO 2 by recyclable organic solvents [9,10] or ionic liquids (ILs) [11][12][13][14][15] has also been proposed by researchers in recent years.…”
Section: Introductionmentioning
confidence: 99%
“…This technology has been widely used in Japan, Taiwan and Southeast Asia, and also in 330 Â 2 MW and 225 Â 2 MW power plants in China. Some studies about MgO WFDG such as the investment [8], the characteristics of the MgSO 3 and MgSO 3 Á6H 2 O [9][10][11], SO 2 absorption in desulfurization system [12,13], the oxidation inhibition of the byproducts [14,15], the byproduct recovering process [16,17], the magnesium-based WFGD process [18,19], and the activity of MgO generated from the decomposition of the by-products [20] have been carried out. Besides, a series of patents have been applied in this area [21][22][23][24][25] To date, the thermal decomposition and kinetics characteristic of the byproducts of MgO FGD from thermal power plant were reported rarely.…”
Section: Introductionmentioning
confidence: 99%
“…Kang (2011) studied the effect of pyrolysis temperature on the activity of MgO generated from the decomposition of the by-products using a pipe furnace. Shen et al (2013) studied the magnesium-based wet FGD process with oxidation inhibition of the by-product. Chen et al (2009) studied the thermo-gravimetric kinetics of MgSO 3 $6H 2 O byproduct from Magnesia wet FGD.…”
Section: Introductionmentioning
confidence: 99%