CONVERSION AND REACTOR SIZING
CONVERSION AND REACTOR SIZING
CONVERSION AND REACTOR SIZING
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One can approximate a PFR by a large # of CSTRs in series:<br />
F A0<br />
1 2 3 4<br />
PFRs in Series<br />
X 2<br />
-r A1<br />
F A1<br />
X 1 =0.4<br />
X1<br />
X 2<br />
∫ ∫ ∫ −<br />
⋅ +<br />
FA0<br />
⋅ = FA0<br />
⋅ FA0<br />
− r − r<br />
0<br />
dX<br />
A<br />
0<br />
-r A2<br />
dX<br />
F A2<br />
X 1 = 0.8<br />
A<br />
dX<br />
r<br />
X1 A<br />
Reactors in Series: CSTR – PFR – CSTR<br />
-F A0/r A<br />
V<br />
PFR<br />
=<br />
n<br />
∑<br />
i=<br />
1<br />
V<br />
CSTR , i<br />
V TOTAL = V PFR,1 + V PFR,2<br />
The overall conversion of<br />
two PFRs in series is the<br />
same as one PFR with the<br />
same total volume<br />
Using the data in the table, calculate the reactor volumes V 1, V 2 and V 3<br />
for the CSTR/PFR/CSTR reactors in series sequence along with the<br />
corresponding conversion.<br />
X<br />
16