3. (25 points) Note the 3 reactions (1 reversible) carried out in a continuous stirred tank reactor (CSTR) shown in the figure below: C. TA C.C.C. The reactions and their rate expressions are: r1 = k1CA A2B AC r2 ky = 1.1 sec-1 k2 = 0.25 liters gmole05 - S r2 = k C 1.5 Iz = kzCc? k3 = 0.06 liter gmole-s B**c+D rn = k CB? ku = 0.35 liter gmole-s The mass balance can be written for the 4 reactions as follows: OUT = IN + GENERATION (Component A) CQ=CAO + Very) (Component B) CQ = 0 + V (27) (Component() CO = 0 + Vyra +74 (Component D) COQ = 0 + V) CONSUMPTION - Vx+3) Vera) Vply) -0 Assuming a reactor volume VR of 1800 liters and an initial concentration of A (i.c Cao) equal to 2.0 gmole/liter, find the overall conversion of A (defined below) as a function of the volumetric flow rate Q varied between 50 & 500 liters/s in increments of 5 liters/s. Plot this relationship in a labeled plot nad print the concentrations for each of the 4 components at Q=50 and Q=500 liers/s.. The conversion of A can be defined as: (CAO-CA) Use the Matlab function fsolve for this problem. For initial concentrations you may assumem CA=CB-Cc-Co=0.4