Question

Equation (8.4) defines the average concentration, $a_{\text {out }}$, of material flowing from the reactor. Omit the $V_z(r)$ term inside the integral and normalize by the cross-sectional area, $A_c=\pi R^2$, rather than the volumetric flow rate, $Q$. The result is the spatial average concentration $a_{\text {spatial }}$, and is what you would measure if the contents of the tube were frozen and a small disk of the material was cut out and analyzed. In-line devices for measuring concentration may measure $a_{\text {spatial }}$ rather than $a_{\text {out }}$. Is the difference important? (a) Calculate both averages for the case of a parabolic velocity profile and first-order reaction with $k \bar{t}=1.0$. (b) Find the value of $k \bar{t}$ that maximizes the difference between these averages.

   Equation (8.4) defines the average concentration, $a_{\text {out }}$, of material flowing from the reactor. Omit the $V_z(r)$ term inside the integral and normalize by the cross-sectional area, $A_c=\pi R^2$, rather than the volumetric flow rate, $Q$. The result is the spatial average concentration $a_{\text {spatial }}$, and is what you would measure if the contents of the tube were frozen and a small disk of the material was cut out and analyzed. In-line devices for measuring concentration may measure $a_{\text {spatial }}$ rather than $a_{\text {out }}$. Is the difference important?
(a) Calculate both averages for the case of a parabolic velocity profile and first-order reaction with $k \bar{t}=1.0$.
(b) Find the value of $k \bar{t}$ that maximizes the difference between these averages.
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Chemical Reactor Design, Optimization, and Scaleup
Chemical Reactor Design, Optimization, and Scaleup
Bruce Nauman 1st Edition
Chapter 8, Problem 5 ↓

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We have a parabolic velocity profile in a cylindrical reactor, which can be expressed as \( V_z(r) = V_{max} \left(1 - \left(\frac{r}{R}\right)^2\right) \), where \( V_{max} \) is the maximum velocity at the center of the reactor, \( r \) is the radial position,  Show more…

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Equation (8.4) defines the average concentration, $a_{\text {out }}$, of material flowing from the reactor. Omit the $V_z(r)$ term inside the integral and normalize by the cross-sectional area, $A_c=\pi R^2$, rather than the volumetric flow rate, $Q$. The result is the spatial average concentration $a_{\text {spatial }}$, and is what you would measure if the contents of the tube were frozen and a small disk of the material was cut out and analyzed. In-line devices for measuring concentration may measure $a_{\text {spatial }}$ rather than $a_{\text {out }}$. Is the difference important? (a) Calculate both averages for the case of a parabolic velocity profile and first-order reaction with $k \bar{t}=1.0$. (b) Find the value of $k \bar{t}$ that maximizes the difference between these averages.
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