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I only need the developed equations! (FP) spec 8 8 Figure P3.7.10 Schematic of two isothermal CSTRs in series. P3.7.10** Develop the set of dynamic

I only need the developed equations!

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(FP) spec 8 8 Figure P3.7.10 Schematic of two isothermal CSTRs in series. P3.7.10** Develop the set of dynamic equations that describe two isothermal CSTR's in series shown in Figure P3.7.10 using an actuator/process/sensor modeling approach. Assume that a single irreversible reaction occurs in this system given by A-" B where r= k C? where k=1 l/gmol-s. Assume that the feed rate to the first reactor is the input variable and that the flow controller on the feed has a time constant of 2 seconds. Assume that the Fs in Figure P3.5.10 represent volumetric flow rates and each has a value of 10 l/s while the volume of each reactor is 100 1. The inlet feed contains only component A at a concentration of C (3 gmol/l). The output variable of this process is the concentration of B in the outlet product stream and the IR analyzer on this stream has a time constant of 30 s. Also assume perfect level control in each reactor (i.e., the flow rate out of the reactor equals the flow rate into the reactor). Identify the dependent variables, the independent variables and the parameters for this model. Initially, each reactor has a concentration of A equal to 3 gmol/l with no product B present and at time equal to zero a catalyst is added to both reactors that allows the reactions to occur. Using a MATLAB or Python program to apply your model, determine the measured concentration of component B in the product leaving the second reactor from time equal to zero to 200 s

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