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which are presented in Table 1. The operating conditions of the gasifier, provided in Table 2, shows that 150l b h of biomass was fed to the gasifier which is operating at 1,600degrees F. Feedstock - Biomass Feed Rate, l b h Equivalence Ratio Oper-atingTemper&ue, F Operating Pressure Bed Material Oxidizing Medium ProductGasFlowrate, scfm -. ~- Pine 150 0.32 1,600 Atmospheric Sand Air 128 -_ I-_ The equivalence ratio was maintained at 0.32 by controlling the amount of fluidization air (oxidizing medium) supplied to the reactor. The temperature profiles along the length of the gasifier are presented in Figure 9. As shown in the plot the gasification fluidization temperature (Pen2)wasmaintainedaround1,600degreesF. Inaddition,thepressureinthegasifierwas maintained between 0.2-0.4 as shown in Figure 10. PD.8360793.2 15PDF Image | THE APPLICATION OF KENTUCKY POWER
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