I need help on e. f. and g.

You are asked to select and size reactors to isothermally carry out a liquid phase, irreversible, reaction AB with the following kinetics: rA=kcA2 where k=0.2L/ (molmin) a. Starting with a mole balance (and assumptions), calculate the time that it would take a batch reactor to process your feed to achieve 95% conversion. The batch reactor is initially charged with 10mol of pure A and the reactor size is 2L. [20 min] b. Starting with a mole balance (and assumptions), calculate the residence time it would take a PFR to process your feed to 95% conversion. The PFR has an inlet feed of pure A at a rate of 10mol/min and the volumetric flow rate is 2L/min. [20 min ] Compare your results in parts A and B and explain their relationship. Starting with a mole balance (and assumptions), calculate the volume it would take for a CSTR to process your feed (from part B) to achieve 95\% conversion. [800 L] e. Calculate the residence time for the CSTR in part D and compare it with part B. Which reactor will you use and why? Which reactor yields the higher conversion given the same residence time. [400 min] f. If the reaction exhibited negative second-order kinetics, does this change your reactor decision and why? g. If the given reaction exhibited zero-order kinetic behavior, does this influence your decision from part E? Why? You are asked to select and size reactors to isothermally carry out a liquid phase, irreversible, reaction AB with the following kinetics: rA=kcA2 where k=0.2L/ (molmin) a. Starting with a mole balance (and assumptions), calculate the time that it would take a batch reactor to process your feed to achieve 95% conversion. The batch reactor is initially charged with 10mol of pure A and the reactor size is 2L. [20 min] b. Starting with a mole balance (and assumptions), calculate the residence time it would take a PFR to process your feed to 95% conversion. The PFR has an inlet feed of pure A at a rate of 10mol/min and the volumetric flow rate is 2L/min. [20 min ] Compare your results in parts A and B and explain their relationship. Starting with a mole balance (and assumptions), calculate the volume it would take for a CSTR to process your feed (from part B) to achieve 95\% conversion. [800 L] e. Calculate the residence time for the CSTR in part D and compare it with part B. Which reactor will you use and why? Which reactor yields the higher conversion given the same residence time. [400 min] f. If the reaction exhibited negative second-order kinetics, does this change your reactor decision and why? g. If the given reaction exhibited zero-order kinetic behavior, does this influence your decision from part E? Why