Problem Scenario A-Model Prediction and Analysis An isothermal constant volume batch reactor was used to carry out multiple runs of the liquid phase reaction (results in Table A-1); A28-C Table A-1 Concentration profile for reactions offerent temperatures and starting me Run 1 2 3 4 5 Temperature 298 298 298 308 318 admol dmmin" 7.25 x 10-2 0.258 0.580 1.37 3.06 Ce moldm) 3.00 4.00 6.00 6.00 6.00 Time (min CA moldml 0 1.00 200 200 200 200 0.88 1.78 1.60 120 0.84 2 0.78 1.30 0.89 3 0.70 1.10 0.70 0.37 0.65 140 1.00 0.57 0.28 5 0.60 1.32 0.85 0.48 0.21 0.55 1.25 0.75 0.40 0.17 0.52 120 0.70 0.35 0.13 0.48 1.15 0.65 0.30 0.11 9 0.45 1.10 0.60 027 0.00 10 1.00 0.55 0.24 0.07 (a) Use the available information to confirm that the reaction is elementary and determine the Authenius constant (mol Adm) min' and Activation Energy u mor for the rate constant Maars Ks+S Data Section Monod Kinetic Model Maintenance Consideration -Is Yo'x+mx Px mX u = specific growth rate [n") max = maximum specific growth rate [h=') Ks = Monod saturation constant [gr'] SEL-malate concentration [gr] X = cell mass concentration (OD) m = Maintenance coefficient [g (OD - 1)-th-'] Yo = True yield of cell mass with respect to L-malate (COD-1 g=