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TEST DESCRIPTION SECTION 3.0 <br /> 3.3.4 Total Gaseous Non-Methane Organics <br /> Concentrations of non-methane hydrocarbons were determined by SCAQMD Method <br /> 25.2, which includes total carbon analysis using special GC techniques. Triplicate samples were <br /> collected into Tedlar bags using a lung sampler. The bags were analyzed by AtmAA laboratory <br /> in Chatsworth, California, within 72 hours of sampling. <br /> 3.3.5 Volumetric Flow Rate and Moisture Content <br /> Stack gas flow rate and moisture content were determined by CARB Methods 2 and 4 <br /> in conjunction with every particulate test, and additionally as needed for the Relative Accuracy <br /> tests. The additional tests included separate picot tube traverses, and moisture determinations <br /> from the Sulfur Oxides sampling trains. <br /> 3.3.6 Fuel An sis <br /> During each test day, composite fuel samples were taken and analyzed for higher heating <br /> value and for C, H, O, N, S, and moisture content. The fuel analysis results are presented in <br /> Appendix C.7. The results were used to calculate fuel "F" Factors according to EPA Method <br /> 19. <br /> 3.3.7 SO, Removal Efficiencv <br /> The coal-filed cogeneration boiler includes systems for removal of SO2 emissions. The <br /> efficiency of those removal systems has been calculated for comparison with permit conditions. <br /> The removal efficiency was calculated using the following equation. <br /> Efficiency = (Cm - C.") * 100 <br /> Cm <br /> Where C = SO2 lb/hr, at the Inlet or Outlet <br /> The mass flow of uncontrolled SO2 emissions was calculated from the fuel flow data for <br /> each test run and from the sulfur content of the fuel (fuel analysis data). The mass flow of <br /> controlled SO2 emissions was provided by the measured stack gas concentration and volumetric <br /> flow rates for each test run. See Appendix D for detailed calculations. <br /> 302108/R143B179.N <br /> 1_J CARAlT <br />