Page 115 - New Trends In Coal Conversion
P. 115

78                                             New Trends in Coal Conversion



                  Table 3.5 Distribution of trace elements in the inlet and outlet of an
                  electrostatic precipitator system
                                                        Removal
                                     Inlet    Outlet    efficiency (%)
                   Particle (size mm)  20     3.57      99.54
                   As                141.5    181.4     99.33
                   Be                13.3     15.1      99.41
                   Cd                1.9      5.2       98.57
                   Cr                361.7    406.1     99.41
                   Mn                311.6    411.0     99.31
                   Ni                140.6    622.6     97.68
                   Pb                167.9    277.2     99.13
                   Sb                9.2      12.9      99.26
                   Se                3.4      29.4      95.49


         firing Eastern (Western Kentucky) bituminous coals have shown that mercury capture
         can increase with increasing fly ash carbon content and decreasing gas temperature
         (Newman-Sutherland et al., 2001). Baghouses can be more effective for mercury con-
         trol than ESP, especially with bituminous coals, as the filter cake on the baghouse acts
         as a fixed-bed reactor for unburnt carbon to enhance mercury capture. Native capture
         for mercury in baghouse systems ranges from low to over 90%, again depending on the
         coal and combustion conditions (Srivastava et al., 2006).


         3.5.2  Flue gas desulfurization
         TEs that are not captured in the ESP or FF device may be removed by a downstream
         FGD system for SO 2 control. The most widely used FGD system is the wet scrubber
         technology followed by spray dry scrubbing and to a lesser extent sorbent injection. At
         this point, it is important to remember that TEs may also be introduced into the FGD
         unit in the limestone. These include, in decreasing order, Ca, Pb, Mn > Cd, Mg, Fe, Si,
         Sm > Ti, Al, W, As, and Sb. TEs may also be introduced by the process water (Sloss
         and Smith, 2000).
            The relatively low temperatures found in WFGD systems allow many of the more
         volatile TEs to condense from the vapor phase and thus be removed from the flue gases
         (Pacyna, 1997).
            Meij (1997) has studied TE removal in the FGD system in unit 13 of the Gelderland
         power plant in the Netherlands. Although the data are for 1986, and somewhat dated,
         they still represent one of the most detailed studies in the literature today. In addition to
         showing gaseous concentrations before and after the FGD unit, the table also demon-
         strates the decrease of 90% in particulate loading across the FGD. Adding this to the
   110   111   112   113   114   115   116   117   118   119   120