the aqueous reaction A + B -> Product, with known kinetics -rA=500(lit/mol*min) CACB, is to take place in an experimental tubular reactor (assume plug flow), under the following conditions: Reactor volume (V)= 0.1 liter Volumetric flowrate (v0)=0.05 lit/min, concentration of reactants CA0=CB0=0.01 mol/lit a) what fractional conversion of reactants can be expected ? b) for same conversion in part (a) what size of stirred tank reactor is needed?