The exit Experiments are being performed using a reactor with non-ideal flow. concentration in response to...

 

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The exit Experiments are being performed using a reactor with non-ideal flow. concentration in response to a pulse input with an inlet volumetric flow rate of 0.1 L/s is given below. C =0 C=0.5t - 1.5 C = -t +6 C =0 C has units of mol/L. a. b. C. d. e. for t <3 s for 3s 6s What is the total amount of tracer fed at t = 0? [0.15 mol] Find an algebraic expression for the residence time distribution function E(t) and graph this as a function of time. Plot F(t) of this reactor to a step change in inlet concentration from 0 to 1 mol/L at t = 0. What is the mean residence time in this reactor? [4.5 s] What is the volume of this reactor? [0.45 L] Using the segregation model of mixing, what is the mean conversion for the second order reaction A B with k = 0.5 L/(mol*s), and CO = 1 mol/L? [0.7] How does this compare to the conversions achieved in a CSTR and a PFR operating at the same residence time? The exit Experiments are being performed using a reactor with non-ideal flow. concentration in response to a pulse input with an inlet volumetric flow rate of 0.1 L/s is given below. C =0 C=0.5t - 1.5 C = -t +6 C =0 C has units of mol/L. a. b. C. d. e. for t <3 s for 3s 6s What is the total amount of tracer fed at t = 0? [0.15 mol] Find an algebraic expression for the residence time distribution function E(t) and graph this as a function of time. Plot F(t) of this reactor to a step change in inlet concentration from 0 to 1 mol/L at t = 0. What is the mean residence time in this reactor? [4.5 s] What is the volume of this reactor? [0.45 L] Using the segregation model of mixing, what is the mean conversion for the second order reaction A B with k = 0.5 L/(mol*s), and CO = 1 mol/L? [0.7] How does this compare to the conversions achieved in a CSTR and a PFR operating at the same residence time?