You are asked to design a reactor to carried out the following reaction: A B where the reaction follows the first order kinetics as: -ra = kCA. The rate constant has a value: k=0.5 min!. Consider that the reaction is carried out in a continuous stirred tank reactor (CSTR), with the concentration of A in the inlet stream at 2 mol/dm and the volumetric flow rates at 5 dm/min for both inlet and outlet streams. For a CSTR of with size of 50 dm?, what conversion is achieved? Assume that no B is present in the inlet stream