Page 261 - Wastewater Solids Incineration Systems
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Incinerator Operations        223




                 An example follows:
                 • Feed rate: 4536 wet kg/h (10 000 lb/hr) or 108 864 wet kg/d (240 000 lb/d)
                 • Dry solids:   33%
                                   (0.33)   (108 864)
                                   35 925 dry kg/d (79 200 lb/d)
                 • Volatile solids: 70%
                                   (0.70)   (35 925 dry kg/d)
                                   25 147 kg/d (55 440 lb/d) volatile solids
                 • Inerts (ash)   35 925   25 147 kg/d   10 778 kg/d (23 760 lb/d)
                 • Heating value   25 575 kJ/kg (11 000 Btu/lb) combustibles (volatile solids)
                 • Q   (Btu   volatile solids/d)/(dry solids/d)
                       (25 575 kJ/kg   25 147 kg volatile solids/d)/35 925 dry solids/d
                       17 902 kJ/kg (7700 Btu/lb) of dry solids
                 • P   (8141)/(17 902   8141) )   100   31% dry solids
                 An incinerator that is operated far below the point of autogenous combustion
             will result in excessive use of auxiliary fuel. Operating far above the point of autoge-
             nous combustion will result in the use of additional cooling air to prevent high incin-
             erator temperatures and clinker formation. Optimum combustion and incinerator
             process control occur when the percentage of solids in the feed cake are at or slightly
             greater than the autogenous combustion point. The theoretical point of autogenous
             combustion should be compared to the actual operational point of autogenous com-
             bustion. To establish autogenous conditions, the operator must frequently observe
             conditions inside the incinerator through a burner view port to watch for signs of
             combustion when auxiliary burners are shut down.
                 Optimum conditions at startup occur when the auxiliary burners are fired to
             match the heat energy required for excess moisture evaporation. When the oper-
             ator observes that feed cake solid ignition has occurred, the auxiliary burners
             should be reduced. The extent of the auxiliary burner reduction depends on the
             heat energy produced from the burning feed. To ensure that the combustion reac-
             tion continues, total heat available from the auxiliary burners and the feed solids
             combustion must be equal to or greater than the heat required for evaporation.
             Therefore, as more of the feed solids mass begins to burn, the auxiliary burners
             should be decreased accordingly.
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