A real tank reactor uses an impeller as a stirrer to carry out an A -> B reaction with a reaction rate constant of k = 0.307 min-1. Before the reactor was put into operation, the residence time distribution of this reactor was checked using a tracer fed into the reactor in a pulse function, the results of which are presented in table 1 below. If the flow rate of component A is 100 kg/hr and the densities and viscosity of compounds A and B are not significantly different ( = 1500 kg/m, = 10-3 Pa. s), design and calculate:

(Distribution of residence time on tracer) a. The average retention time of this reactor. b. The dimensions of the tank if the design of this tank reactor uses a ratio of length (L) and tank diameter (D) is L/D = 1.5 with 30% free volume. c. Power required in a stirred reactor.

Distribution of residence time on tracer k = 0,307 menit^-1 flow rate of component A = 100 kg/hr the densities and viscosity of compounds A and B are not significantly different (density = 1500 kg/m, viscosity = 10-3 Pa. s) that's all the information stated in the question.

t (menit) C (mol/L) 0 0 5 3 10 5 15 5 20 4 25 2 30 1 35 0 t (menit) C (mol/L) 0 0 5 3 10 5 15 5 20 4 25 2 30 1 35 0