A ---> U + S, the following velocity data were obtained for the liquid phase reaction at 40C. This reaction will be carried out to produce 10 kmol of U per day with an input concentration (CAo) of 4 mol/L. According to the conversion of 85% of the input;

Note: There is no need to find a velocity model.

a) If only one backmixing tank is used, the required operating time and reactor volume

b) If a piston flow tank is used, the required operating time and reactor volume

c) the optimum two-reactor system and volumes to be used

d) If KT is used, the reaction time, the number of intermittent operations that can be made in a day and the reactor

volume

\begin{tabular}{c|c|c|c|c|c|c|c|c|c|c} CA:;mol/L & 0.6 & 1.3 & 1.5 & 2.0 & 2.5 & 2.8 & 3.3 & 3.5 & 4.0 & 4.5 \\ \hline- - A Aolmolst & 33.30 & 16.05 & 12.50 & 7.50 & 3.75 & 2.50 & 2.25 & 2.25 & 3.75 & 7.00 \\ \hline & & & & & & & & & & \\ \hline & & & & & & & & & & \end{tabular} \begin{tabular}{c|c|c|c|c|c|c|c|c|c|c} CA:;mol/L & 0.6 & 1.3 & 1.5 & 2.0 & 2.5 & 2.8 & 3.3 & 3.5 & 4.0 & 4.5 \\ \hline- - A Aolmolst & 33.30 & 16.05 & 12.50 & 7.50 & 3.75 & 2.50 & 2.25 & 2.25 & 3.75 & 7.00 \\ \hline & & & & & & & & & & \\ \hline & & & & & & & & & & \end{tabular}