| 1 | \documentclass{article} |
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| 2 | \usepackage{fullpage} |
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| 3 | \usepackage{pstricks} |
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| 4 | \begin{document} |
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| 5 | \begin{enumerate} |
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| 6 | \item Dimensional analysis: catalytic combustion of carbon monoxide |
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| 7 | |
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| 8 | CuO is a good catalyst for the reaction |
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| 9 | $$\rm 2CO(g)+O_2(g)\Rightarrow 2CO_2(g)$$ |
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| 10 | CuO is coated on the internal surfaces of porous Al$_2$O$_3$ spheres of |
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| 11 | radius $R$, so the gases containing CO and O$_2$ can diffuse in through the |
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| 12 | pores with diffusivity $D$ and react on the internal CuO surfaces. (The |
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| 13 | Al$_2$O$_3$ is used as a substrate because of its high strength and stability |
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| 14 | at the high temperatures reached due to combustion; porous CuO would sinter |
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| 15 | into dense solid spheres at such temperatures.) |
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| 16 | |
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| 17 | \begin{center} |
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| 18 | \input{convandsphere} |
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| 19 | \end{center} |
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| 20 | |
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| 21 | Because the pores are a lot smaller than the sphere, you can treat this as a |
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| 22 | homogeneous chemical reaction throughout the porous solid. Assume for this |
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| 23 | problem that O$_2$ is the limiting reagent, and the rate of reaction is |
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| 24 | proportional to its concentration with ``homogeneous'' rate constant $k$, so |
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| 25 | $G=-kC_{\rm O_2}$. The concentration of oxygen in the pores just inside the |
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| 26 | surface of the sphere is approximately equal to that in the gas outside, so |
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| 27 | that is our outer surface boundary condition. |
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| 28 | |
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| 29 | If the concentration of oxygen throughout each sphere is very uniform, then |
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| 30 | the reaction will be occurring on all of the inner pore surfaces within each |
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| 31 | sphere, so the CuO will be well-utilized. On the other hand, if we are |
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| 32 | flowing CO gas through this bunch of spheres, the larger the spheres, the |
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| 33 | less resistance to flow there will be. So we want the spheres to be as large |
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| 34 | as possible without being so large that there is no reaction at their center. |
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| 35 | |
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| 36 | \begin{enumerate} |
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| 37 | \item\label{pi1} Write an expression for a parameter which describes the |
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| 38 | uniformity of oxygen concentration, in terms of the other problem |
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| 39 | parameters. |
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| 40 | |
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| 41 | \item Identify the number of parameters, and the number of independent units, |
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| 42 | and use the Buckingham pi theorem to determine the number of independent |
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| 43 | dimensionless parameters in the problem. |
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| 44 | |
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| 45 | \item Write a new expression for the dimensionless uniformity parameter in |
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| 46 | part \ref{pi1} in terms of the other dimensionless parameter(s). |
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| 47 | |
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| 48 | \item If you double the sphere radius, how much does $k$ have to change in |
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| 49 | order to yield the same uniformity? (The reaction rate coefficient $k$ |
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| 50 | tends to be a much stronger function of temperature than diffusivity, so |
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| 51 | changing the temperature will change $D$ a small amount and $k$ a large |
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| 52 | amount.) |
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| 53 | |
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| 54 | \item Draw a sketch (or sketches) showing how you think that uniformity |
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| 55 | parameter will vary as a function of the other parameter(s), making sure |
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| 56 | your sketch captures the transition from strongly non-uniform to roughly |
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| 57 | uniform concentration in a sphere. |
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| 58 | |
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| 59 | \item Sketch the concentration of oxygen in a sphere as a function of radius |
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| 60 | for large and small values of the other dimensionless parameter(s) of which |
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| 61 | uniformity is a function. If there is more than one such parameter, make |
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| 62 | sketches for all combinations of large and small values of each |
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| 63 | parameter. |
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| 64 | \end{enumerate} |
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| 65 | \end{enumerate} |
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| 66 | \end{document} |
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