CONVERSION AND REACTOR SIZING
CONVERSION AND REACTOR SIZING
CONVERSION AND REACTOR SIZING
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Sizing in PFR<br />
Example: Determine the volume in PFR to achieve a 80 % conversion.<br />
dX<br />
For PFR : FA0<br />
⋅ = −rA<br />
dV<br />
0 0.<br />
8 0 0.<br />
8<br />
dX F FA0<br />
Re arranging : V = FA0<br />
⋅ ∫ = ⋅ dX<br />
− r ∫ − r<br />
Let’s numerically evaluate the integral with trapezoidal rule<br />
0.<br />
8<br />
∫<br />
0<br />
FA0<br />
⋅ dX<br />
− r<br />
A<br />
⇒<br />
FA0<br />
f ( X ) = =<br />
− r<br />
0<br />
A X = 0<br />
FA0<br />
f ( X ) = =<br />
− r<br />
A<br />
A X = 0.<br />
8<br />
0<br />
0.<br />
89<br />
8.<br />
0<br />
0.<br />
8<br />
3<br />
V = ⋅(<br />
0.<br />
89 + 8.<br />
0)<br />
= 8.<br />
89⋅<br />
0.<br />
4 = 3.<br />
556m<br />
2<br />
With five point quadrature V = 2.165 m3 Comparing CSTR & PFR Sizing<br />
V CSTR > V PFR for the same conversion and rxn conditions.<br />
The reason is that CSTR always operates at lowest rxn rate. PFR starts at a high<br />
y p g<br />
rate, then gradually decreases to the exit rate.<br />
A<br />
12