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94          Wastewater Solids Incineration Systems




                    The temperature of the exit gas varies depending on the temperature and quantity of
                    the dilution gas, but is typically in the range of 370 to 870°C (700 to 1600°F).
                        Exhaust gases are ducted into a heat exchanger to recover thermal energy and
                    generate low temperature dilution gas. Several options are available for recovering
                    the heat, including steam generation, thermal oil, and hot gas heat exchangers. After
                    the exhaust gas exits the heat recovery unit, it is split into two directions. Approxi-
                    mately 70% of the exhaust gas flow enters the exhaust gas recirculation (EGR) fan
                    and is injected back into zone 3. The remaining 30% is directed to a fabric filter to cap-
                    ture and remove particulate from the exhaust stream.
                        After exiting the fabric filter, the exhaust is further cooled and water vapor, pro-
                    duced during combustion, is condensed in a packed tower condenser. The exhaust
                    gas is cooled to 32 to 49°C (90 to 120°F) and directed to the gas recycle header where
                    a portion of the exhaust gas—approximately 10%—is vented out of the process to
                    advanced air pollution control equipment. The remaining 20% of recycled gas is
                    boosted in pressure through a recycle fan and enriched with oxygen. The end result
                    is synthetic air which is injected back to zone 1.
                        Heat energy recovered from the system can be transferred directly to a feed
                    drying circuit. In most cases the dry feed cake provides enough thermal energy to
                    eliminate the need for an additional energy source for drying. Figure 5.19 illustrates
                    the thermal energy balance for the process installed at the North Shore Sanitary Dis-
                    trict’s Sludge Recycling Facility, Zion, Illinois.
                        Oxygen can be provided to the process from either on-site liquid storage or gen-
                    eration with either adsorption or cryogenic air separation technologies. Liquid
                    oxygen is vaporized and warmed to ambient conditions to meet process demands.
                        Markets for the glass aggregate product are large and diverse. More than 2.25
                    mil. metric tonnes (2.5 mil. tons) per year of the material is currently produced in a
                    similar industry known as slag marketing. The process of water quenching the
                    molten glass as it exits the system results in the formation of an environmentally inert
                    aggregate. During quenching, heavy metals that may be present are physically
                    sequestered in the glass matrix resulting in low leaching.


                    10.2 Miscellaneous Technologies
                    10.2.1 Gasification
                    Gasification is a process that uses heat, pressure, and steam to convert materials to a
                    gas composed primarily of carbon monoxide and hydrogen (California Integrated
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