??? P2-2 (a) Revisit Examples 2-1 through 2-3. How would your answers change if the flow rate, $F_{A0}$, were cut in half? If it were doubled? What conversion can be achieved in a 4.0 m³ PFR and in a 4.0 m³ CSTR?
(b) Revisit Example 2-4. How would your answers change if the two CSTRs (one 0.82 m³ and the other 3.2 m³) were placed in parallel with the flow, $F_{A0}$, divided equally between the reactors.
(c) Revisit Example 2-5. (1) What would be the reactor volumes if the two intermediate conversions were changed to 20% and 60%, respectively? (2) What would be the conversions, $X_1$, $X_2$, and $X_3$, if all the reactors had the same volume of 100 dm³ and were placed in the same order? (3) What is the worst possible way to arrange the two CSTRs and one PFR?