Page 250 - Boiler plant and distribution system optimization manual
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Waste Heat Recovery                                                                              235



                pated. The cast iron sleeve will corrode, but it can   the metal, or stack wall, that is in contact with the
                be replaced at normal maintenance intervals. The    flue gas that will determine the extent of acid cor-
                cast iron sleeves protect the carbon steel tubes    rosion. Stack insulation will aid in keeping stack
                from contact with corrosive gases.                  temperatures above the ADP.
                                                                         Alternatives to insulation are high tempera-
                Improve Fluid Flow Arrangement                      ture corrosion-resistant stack material such as
                     Using parallel-flow tube arrangements rath-    Cor-Ten or Fiberglass reinforced plastic.
                er  than  counter-flow  arrangements  increases
                economizer  skin  temperature.  With  the  parallel
                flow  arrangement,  cold  feedwater  enters  where   CONDENSING THE MOISTURE IN
                the stack gas is the hottest, thus raising the tube   FLUE GASSES
                surface temperature slightly.
                                                                         The major limitation to increased boiler effi-
                Modulate Feedwater                                  ciencies Is the amount of energy tied up in latent
                Flow through the Economizer                         heat. Until recent years equipment has not been
                     The feedwater flow rate through the econo-     available to capture and use this large source of
                mizer economizer can be controlled by diverting     waste energy. Figure 12.9 shows the energy avail-
                feedwater flow around the economizer during pe-     able in combustion products for natural gas at dif-
                riods of low flue gas temperatures (Figure 12.8).   ferent excess air levels as the temperature drops
                                                                    from 600°F to the point of flue gas condensation
                Insulate Stack Metal                                and full recovery of latent and sensible heat.
                     Just as with metal temperatures in the econ-        For example, 400°F flue gasses from a natu-
                omizer, flue gas temperatures will not necessar-    ral gas fired boiler contains 18% of the total en-
                ily determine the severity of acid corrosion, the   ergy from the HHV of the input fuel in the form
                same is true for the stack. It is the temperature of   of both sensible and latent heat. Almost 62% of





































                                     Figure 12.8—Economizer corrosion control by feedwater bypass.
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