Example 3.10: A flue gas containing 700 lb/h of SO2 and 500 lb/h of HCl enters a dry scrubber where lime feed rate is 1.6 times the stoichiometric requirement. Dry scrubber is 80% efficient in removing SO2 and 90% efficient in removing HCl. How much is the lime addition-rate? What is the mass flow rate of CaO, SO2, HCl, CaSO3, CaCl2 and H2O in the flue gas, leaving scrubber. Assume that CO2 does not react with the lime (CaO).
Solution:
Mass of SO2 = 700 lb = 700/64 = 10.938 lbmol
Moles of SO2 converted = 0.8(10.938) = 8.75 lbmol
Mass of HCl = 500 lb = 500/36.5 = 13.7 lbmol
Moles of HCl converted = 0.9(13.7) = 12.33 lbmol
Stoichiometric requirement of CaO = 1(10.938) + 0.5(13.7) = 17.79 lbmol
Excess of lime to be used = 60%
Actual requirement of lime = 1.6(17.79) = 28.46 lbmol = 28.46(56) = 1593.7 lb
Actual consumption of CaO = 1(8.75) + 0.5(12.33) = 14.92 lbmol = 14.92(56) = 835.24 lb
Total mass = 700 + 500 + 1593.7 = 2793.7 lb
CaO in the product = 1593.7 - 835.24 = 758.46 lb
CaSO3 formed = 8.75 lbmol = 8.75(120) = 1050 lb
CaCl2 formed = 0.5(12.33) = 6.165 lbmol = 6.165(111) = 684.27 lb
Water formed = 0.5(12.33) = 6.165 lbmol = 6.165(18) = 110.96 lb
SO2 unconverted = 0.2(10.938) = 2.188 lbmol = 2.188(64) = 140 lb
HCl unconverted = 0.1(13.7) = 1.37 lbmol = 1.37(36.5) = 50 lb
Total products rate = 758.46 + 1050 + 684.27 + 110.96 + 140 + 50 = 2793.69