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extrapolated to full-scale units. Furthermore, there are significant differences between <br /> kilns and other combustion devices, such as boilers, and the study does not address these <br /> issues. Nevertheless, the simulator is useful in examining the fundamental phenomena of <br /> TDF combustion and to gain an understanding of the qualitative trends that would be <br /> found in a full-scale rotary kiln. <br /> The TDF tested was wire-free crumb rubber sized to <0.64 cm (<1/4 in.). It was <br /> combusted at several combinations of feed rate, temperature, and kiln oxygen <br /> concentration. The TDF was combusted with natural gas as the primary fuel. Samples <br /> were taken to examine volatile and semi-volatile organics, PCDD/PCDF, and metal <br /> aerosols. Data were collected to determine the effects of feed rates, type of feeding, i.e., <br /> continuous versus batch, and combustion controls on emissions. The data were taken in <br /> the exhaust stream prior to any add-on air pollution control devices. <br /> The study addressed two issues: (1) the influence of the mode of tire feeding, for <br /> example, whole tires versus shredded tires, on the PICs, and (2) the potential for air toxic <br /> emissions not normally found when burning conventional fuels. <br /> The TDF material used in the test program was analyzed and the proximate and <br /> ultimate analyses and metals analysis results are presented in Table 17. TDF contains <br /> significant amounts of zinc, since zinc is used extensively in the tire manufacturing <br /> process. <br /> In all, thirty test conditions were run, with the TDF feed rate varying from 0% to <br /> 21.4% of heat input. The test conditions were achieved by varying kiln firing rate, <br /> combustion air flow rate, and tire feed rate. The majority of the tests were conducted with <br /> a steady-state feed of TDF. Variations in the mode of TDF feeding were evaluated in two <br /> tests. In one test, the kiln air flow rate was ramped up and down every 10 minutes <br /> ("ramp") to change the kiln oxygen concentration to simulate transient operation. In the <br /> other, TDF was introduced in 300 g batches spaced ten minutes apart ("batch") to <br /> simulate transient operation, such as feeding whole tires at periodic intervals. <br /> VOCs were collected by a Volatile Organic Sampling Train (VOST) and analyzed <br /> with a gas chromatograph/mass spectrometer (GC/MS). The majority of the VOCs were <br /> very near to or below the detection limits of the equipment. Estimated emissions of VOCs <br /> for five representative test runs are presented in Table 18. <br /> PAHs were analyzed with a Continuous Emission Monitor (CEM) PAH analyzer. <br /> PAH emissions were fairly insensitive to temperature and oxygen for the range of <br /> conditions studied, however, increasing TDF feed rates tended to increase PAH emissions <br /> for all oxygen levels. Overall, it was observed that supplementing natural gas with TDF <br /> tended to increase PAH emissions, but not dramatically, provided that steady-state <br /> operation is maintained. <br /> Semi-volatile organic compounds (SVOC) and bulk particulate were collected by <br /> isokinetic sampling protocols with a Modified Method 5 (MM5) train. Data from the <br /> analyses did not indicate that SVOC were present in detectable concentrations. Lemieux <br /> 32 <br />