A second order, elementary reaction 2AB occurs in a liquid phase CSTR, with the reaction rate constant k=0.16 L.mol-1.s-1. The feed concentration of A, CAo, is 0.88 mol.L-1, the feed flowrate is 35 L.s-1 and a conversion of 48% is achieved. (Give all answers to 4 significant figures until the final answer). What is the molar flowrate of A in the reactor feed? mol/s What is the molar flowrate of A in the reactor outlet? mol/s What is the concentration of A in the reactor outlet? mol/L Calculate the rate of reaction or A in the CSTR. mol.L-1.s-1 What is the required reactor volume? Give the final reactor volume, taking into account the significant figures: If a second CSTR is added in series so that the overall conversion is 68% : What is the concentration of A at the exit of the second reactor? (Give all answers to 4 significant figures until the final answer). What is the concentration of A at the exit of the second reactor? (Give all answers to 4 significant figures until the final answer). mol/L Calculate the rate of reaction of A in the second CSTR. mol.L-1.s-1 Calculate the concentration of B at the exit of the second reactor. mol/L Calculate the reactor volume of the second reactor. L Give the final volume for the second reactor, taking into account the significant figures: L