Not Reacted Core Model Applied in Palm Nut Shell Pyrolysis

<div>Comparison between experimental conversion in the rotary kiln (<i>χ</i>) with lifters and conversion calculated with the Not Reacted Core model (<i>d</i><sub>80</sub> = 12 mm; feed = 900 kg/h; <i>T</i> = 850°C; <i>n</i> = 2.9 rpm).</div>

International Journal of Chemical Engineering

fig7

Figure 7

Figure 7: Not Reacted Core Model Applied in Palm Nut Shell Pyrolysis 