c) A packed bed reactor of 0.30m diameter and 3.0m height was designed as a plug flow reactor and is used for decomposing of 40L min1 microfluid with the rate: rA=kCA2. i) What is the maximum initial concentration of A enabling 85% conversion if the reaction constant k=0.6Lmol1min1 and the packing occupies 50% of the reactor volume? [15\%] ii) The subsequent measurement of the residence time distribution is shown in Fig. 2. Sketch the combination of compartments that would give this residence time distribution. [20\%] iii) Calculate the conversion in the real reactor. Fig. 2. Residence Time Distribution measured in the real reactor