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10.3  Flue Gas Desulfurization                                  291

            Table 10.3 The most important FGD systems with regenerable sorbents
            Process                   Sorbent/principle          End/by—product
            Wellman—Lord              Sodium sulfite (Na 2 SO 3 )  Concentrated SO 2
            Bergbau Forschung/Uhde    Activated carbon           Concentrated SO 2
            Linde SOLINOX             Physical absorption (amine)  Concentrated SO 2
            Spray-dry scrubbing       Sodium carbonate (Na 2 CO 3 )  Elemental sulfur
            MgO process               Magnesium oxide (MgO)      Concentrated SO 2


              Wellman-Lord process [23] is the most widely used wet renewable sorbent FGD
            process. Sodium carbonate, Na 2 CO 3 is the actual sorbent and NaHSO 3 is the
            product of reaction.

                              Na 2 CO 3 þ SO 2 þ H 2 O ! 2NaHSO 3       ð10:14Þ

              The sulfur is released again as SO 2 , which is extracted as a mixture of
            approximately 85 % SO 2 and 15 % water. The mixture can be further processed to
            sulfuric acid.

                               NaHSO 3 ! Na 2 SO 3 þ SO 2 þ H 2 O       ð10:15Þ
                                      1
                                 SO 2 þ = 2O 2 þ H 2 O ! H 2 SO 4       ð10:16Þ
              Some sodium sulfite/sulfate is formed as a by-product; make-up soda or trona is
            needed to balance this loss. Make-up Na 2 CO 3 (soda) or Na 2 CO 3 · NaHCO 3 (trona)
            is necessary to compensate the loss of sodium from the system with the CaSO 3 /
            CaSO 4 product. Therefore, an actual process includes a more concentrated sodium-
            based liquid with limestone/lime scrubbers, combined with precipitation and
            regeneration in separate devices.



            10.3.2 Steam Reactivation of Calcium Based Sorbents


            Since the molar volume of CaSO 3 or CaSO 4 is higher than molar volume of CaO or
            Ca(OH) 2 , the volume of sulfation products shall be greater than the volume of
            sorbent consumed. This result in a progressive pore blockage that gradually elim-
            inates the access of SO 2 to the active CaO surface. Due to this pore eliminating
            phenomena, only a fraction of the CaO is utilized in sulfation. The low conversion
            rate of sorbent results in not only a waste of resource and low efficiency in FGD, but
            also increased particulate contaminants in the gas stream and consequently the
            increased burden for the particulate separation units and sludge treatment.
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