Page 321 - Air pollution and greenhouse gases from basic concepts to engineering applications for air emission control
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298                                 10  Post-combustion Air Emission Control

            absorption/adsorption methods have been introduced in Part 1. SO x /NO x removal
            by electron beam radiation is briefly introduced by [13]. SO 2 /NO X can also be
            captured by copper oxide spray mixed with ammonia. SO 2 is first captured CuO at
            400 °C.

                                             1
                                CuO þ SO 2 þ = 2O 2 ! CuSO 4            ð10:26Þ
                                   CuO þ SO 2 ! CuSO 3                  ð10:27Þ

                                   CuO þ SO 3 ! CuSO 4                  ð10:28Þ
              Meanwhile, NO is reduced by ammonia to nitrogen, for which copper oxide is a
            very good catalyst.

                              4NO þ 4NH 3 þ O 2 ! 4N 2 þ 6H 2 O         ð10:29Þ
                            2NO þ 2NH 3 þ O 2 þ H 2 ! 2N 2 þ 4H 2 O     ð10:30Þ

              The copper sulfate (CuSO 4 ) product is transported to the two-stage heater/
            regenerator section where it is reduced to Cu at 500° C. SO 2 is released and it also
            can be used for sulfuric acid production.
              More recently, researchers are trying to use wet scrubbers to absorb both SO 2 and
            NOx simultaneously, in this approach, the caustic solution contains strong oxidizers
            [39] and the oxidants include Fe(II)-EDTA and H 2 O 2 , penta- and hex-amminecobalt
            (II) chloride [37, 38]. Penta- and hexa-amminecobalt(II) chloride seemed to be
            superior over other two oxidants, but they are not stable and cannot be stored for
            long time. More importantly, waste disposal is a major challenge when cobalt is
            mixed with fly ash in the sludge and dissolved in the liquid solvent.




            10.6 Control of Volatile Organic Compounds


            The properties of the VOCs determine the suitable methods to capture or to oxidize
            the VOCs in a gas stream. The most important parameter is the flammability limits,
            also referred to as flammable limits of the VOCs/Air mixture. The lower flammable
            limit (LFL) describes the mixture with the smallest fraction of combustible gas. The
            upper flammable limit (UFL) defines the richest flammable mixture. These limits
            define whether the air-VOCs mixture may ignite or not [5]. When the mixture
            exceeds 25 % of the LFL, there is a high chance of ignition and it has to be handled
            with caution. The values of LFL and UFL for several VOCs and other gaseous
            organic compounds are available in literature [18]. For gas mixtures with VOC
            contents below LFL, the most important options are VOC combustion, condensa-
            tion, and carbon absorption. When the concentration of VOC is above the UFL the
            gas can be oxidized in flares or boilers with air or steam.
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