Page 151 - Wastewater Solids Incineration Systems
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118         Wastewater Solids Incineration Systems




                    of the fluid bed are 820 to 870°C (1500 to 1600°F), with excursions to 930°C (1700°F)
                    or higher. A typical temperature range of preheated air is 540 to 650°C (1000 to
                    1200°F); however, this can rise even higher during furnace temperature excursions.
                    Although the feed cake is dewatered before incineration, fluid bed furnace exhaust
                    flue gases still contain approximately 35 to 45% water vapor by volume.
                        Fluid bed incinerators must, by function, operate as an oxidizing environment
                    with excess air rates of 40% or greater; however, occasional upsets may create
                    reducing environments. This situation not only aggravates corrosion but also intro-
                    duces the risk of after-combustion in the heat exchanger and connecting ductwork.
                    Chlorides in the feed cake are another common source of corrosion attack. The typ-
                    ical composition of flue gases was discussed in section 2.3 of this chapter.
                        Many incinerators are run on a demand basis rather than continuously.  A
                    common operating cycle follows the normal working week: 8 hours per day; 5 days
                    per week; or, in some cases, 24 hours per day, 5 days per week. Such cyclic operation
                    can be damaging, both from mechanical stress and materials wear. Repeated transi-
                    tions through the dewpoint range are particularly harmful because this can cause
                    corrosive condensation, deposits, and potential plugging problems. If lime is intro-
                    duced to the feed cake for sulfur control, then plugging can be further aggravated,
                    which can lead to corrosion, erosion, and mechanical problems.

                    4.1.2 Air Preheater Design
                    With an FGTT design, each tube is fitted with an expansion joint to allow differential
                    thermal movement between individual tubes. As shown in Figure 6.5, large main expan-
                    sion joints compensate for differential movement between the tube bundle and the cool,
                    refractory-lined shell. Most modern expansion joint bellows are made of Alloy 625.
                        A typical FGTT recuperator may have 91 tubes of type 304 stainless steel or alloy
                    20, arranged on a triangular pitch. Tube (pipe) size may be 9 m long   89 mm diam-
                    eter   3 mm wall thickness (30 ft   3.5 in   0.120 in). Units have been built with as
                    few as 19 and as many as 162 tubes. Pipe sizes range from 50 to 200 mm (2 to 8 in) in
                    diameter, illustrating the range of the preheater supply and capacity.
                        Tubes are welded directly to the tube sheet. Alloy or stainless steel is typically
                    specified for the upper tube sheet, which is exposed to the full temperature of the hot
                    air and supports the entire tube bundle. The shell, flue gas plenums, and lower tube
                    sheet are carbon steel. Insulating refractory linings are typically required for the
                    entire casing and hot face on the tube sheets. Dense, abrasion-resistant refractories
                    help avoid erosion by the particulates in the flue gas. Vapor barriers or coatings on
                    interior carbon steel surfaces minimize acid attack on flue gas plenums.
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