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Show (Table IV), by adding N2 diluent to the fuel stream or to the air stream while maintaining the fuel and air flowrates fixed. Emissions measurements and flame photographs were obtained for various levels of dilution. TABLE IV. Baseline Experimental Flame Conditions (No Diluent) Fuel Temperature (K) Air Temperature (K) Fuel Flowrate (mg/s) Air Flowrate (mg/s) Mean Fuel Velocity (cm/s) Mean Air Velocity (cm/s) Unheated Reactants 293 293 3.0 243 5.0 2.4 Heated Reactants 413 398 3.3 243 7.8 3.5 NO, NOx and CO emission indices were calculated from measured mole fractions of NO, NOx, CO, and C02 in the product gases [11]. Visual flame length measurements were obtained from color flame photographs. Although all flames were nonsooting, i.e., no soot escaped the flame, the appearance of a yellow luminosity indicated the presence of in-flame soot. Typically, the region closest to the fuel tube exit was blue (soot free), while the remainder of the flame exhibited a yellow luminosity. This soot-free length of the flame at each condition also was measured. Results and Discussion NOx emission indices and visible flame lengths are shown as functions of diluent fraction in Fig. 9 for the flames with heated reactants. Here we see that air dilution was more effective than fuel dilution in reducing NOx emissions. We also see that visible flame lengths increased somewhat as diluent was added to the air stream, while no effect on flame length was observed for fuel dilution. Similar trends were found for both NOx and flame lengths for the flames with unheated reactants; the effects, however, were less pronounced. Flame length trends with diluent addition are nominally consistent with the theoretical predictions of Roper [13,14]. Using Roper's analysis, we predict that the addition of diluent to Z = 0.15 should result in an increase in flame length of 15% for air dilution and an increase of 8% for fuel dilution. The experimental visible flame lengths showed increases of 18% and 0%, respectively, while flame lengths based 11 |