obtain a transfer function relating the output Cb and the input F

F = (16) V C1 = -kCA k3C; + (Cas C) CB = k CA - k2CB - F CB V (17) = where CA and CB denote the concentration of components A and B respectively. The model parameters and nominal operating conditions are: ki = 50 h-?, k2 = 100 h-?, kz = 101 mol-'h-?, Car= 10 mol/L, V = 1 L, X1=CA= 3.0 mol/L, X2 = CB=1.12 mol/L and u=F= 34.3 L/h. The control problem is to regulate CB by manipulating the inlet flow rate (F). The operating space considered here