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272                                   9 In-combustion Air Emission Control

            Table 9.1 Comparison of in-furnace Low-NO x technologies
            Technology          Advantage                       Disadvantage
            Low excess air                                      Fuel burnout
                                                                decreases
            Low-NO x burner (i.e.,  Always for NO x reduction   Minor decrease in
            fuel staging in flame)                               fuel burn-out
            Air staging         Always for NO x reduction       Increased risk for
                                                                corrosion, slagging
            Fuel staging in furnace  Always, especially when the reburn fuel is  High capital cost
                                the same as the fuel in first stage
            Flue gas recirculation  Effective for high-temperature oil or gas  Low efficiency
                                fired furnaces


            9.4.4 Combined Low-NO Technologies
                                     x

            Table 9.1 summarizes the comparison of the in-furnace low-NO x technologies.
            Each of the methods has its pros and cons. In order to achieve the best NO x
            reduction performance, a combination of the low-NO x methods described above can
            be employed. A typical combination is illustrated in Fig. 9.11 above.
              The actual selection and combination of low-NO x combustion technologies
            depends on the fuel and the boiler itself. When combining several in-furnace
            measures for coal fired boilers, only 70 % or less of the total NO x reduction can be
            achieved. The major reason for the limited NO x reduction is that these in-com-
            bustion technologies mainly control the NO x related to the nitrogen compounds
            released from the fuel at the early stage of the combustion, or in short, volatile-N.
              Not all the fuel nitrogen is released during this stage, and 20–80 % may remain in
            the fuel forming char-N, which is converted to NO x in the flue gas. The char-N
            content is largely unknown and varies from fuel to fuel and from furnace to furnace.
            Current low-NO x methods are capable of controlling almost 100 % of the NO x from
            volatile-N. Therefore, additional post-combustion NO x control is necessary to fur-
            ther remove the NO x from the flue gas before being discharged into the atmosphere.



            9.5 In-combustion Soot Control

            Soot formation can be reduced by controlled turbulent mixing, which promotes more
            complete combustion [3, 7, 8]. Additives to the fuels such as iron, nickel, manga-
            nese, or cobalt act as catalyst, can further improve the oxidation of soot, however,
            sometime these additives may also increase the production of soot. Feitelberg et al.
            [6] reported that additives of iron and manganese increased the production of soot up
            to a factor of 3 under all combustion conditions. They found that these additives did
            not affect soot particle collision rate or inception.
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