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                    Thermal Oxidation                                                         349





















                                        Fig. 2. Thermal incinerator. (From US EPA.)



                    in this chapter will be based on thermal incineration systems where the emission
                    streams are preheated.
                       The incineration of emission streams containing organic vapors with halogen or sulfur
                    components may create additional control requirements. For example, if sulfur and/or
                    chlorine are present in the emission stream, the resulting flue gas will contain sulfur
                    dioxide (SO ) and/or hydrogen chloride (HCl). Depending on the concentrations of
                               2
                    these compounds in the flue gas and the applicable regulations, scrubbing may be
                    required to reduce the concentrations of these compounds. The selection and design of
                    scrubbing systems are discussed in another chapter.
                       In this chapter the calculation procedure will be illustrated using emission stream
                    1 described in Table 1. Example 1 contains worksheets for design and technical cal-
                    culations (4).
                    1.2. Range of Effectiveness
                       Thermal incineration is a well-established method for controlling volatile organic
                    compound (VOC) emissions in waste gases. The DE for thermal incineration is typically
                    98% or higher. Factors that affect DE include the three “Ts” (temperature, residence
                    time, and turbulence) as well as the type of contaminant in the waste gas. With a
                    0.75-s residence time, the suggested thermal incinerator combustion temperatures
                    for waste  gases containing nonhalogenated VOCs are 1600ºF and 1800ºF, respec-
                    tively, for 98% and 99% VOC DEs. Higher temperatures (about 2000ºF) and longer
                    residence times (approx 1 s) are required for achieving DEs of 98% or higher with a
                    halogenated VOC (4,12).
                    1.3. Applicability to Remediation Technologies
                       Storage tanks and surface impoundments are the major sources of organic air emis-
                    sions at hazardous waste treatment, storage, and disposal facilities, and Superfund sites.
                    Based on work performed in the development of the benzene waste National Emission
                    Standards for Hazardous Air Pollutants (NESHAP), wastewater systems are a major
                    source of benzene emissions from wastes that contain benzene (8–11).
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