•  use Matlab and the graphs should be somewhat similar to the screenshot(2nd one) shown below). The reactor temperature (T), rate constant (kf), equilibrium constant (K), and the differential form of the fraction of conversion are shown below.

 

Transcribed Image Text:

dfA -rA FAO dv = (1) T330 +43.4fA (2) kf = 33.1 exp | 7906 3 exp[-8 K = 3.03 exp-830.3 T-360 1360)] 360T T-333 333T (3) )] (4) a) Using the initial conditions: V=0, fA=0. Using Matlab, or other ODE solver, plot the fraction of conversion (fA), T, and -A as a function of cumulative volume (V). You can set the volume of the reactor to 4 m. b) What is the volume of the PFR corresponding to the maximum rate of reaction (-A). How much higher is the temperature at the outlet (V=4 m) compared to the inlet? dfA -rA FAO dv = (1) T330 +43.4fA (2) kf = 33.1 exp | 7906 3 exp[-8 K = 3.03 exp-830.3 T-360 1360)] 360T T-333 333T (3) )] (4) a) Using the initial conditions: V=0, fA=0. Using Matlab, or other ODE solver, plot the fraction of conversion (fA), T, and -A as a function of cumulative volume (V). You can set the volume of the reactor to 4 m. b) What is the volume of the PFR corresponding to the maximum rate of reaction (-A). How much higher is the temperature at the outlet (V=4 m) compared to the inlet?