| 1 | \documentclass{article} |
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| 2 | \usepackage{fullpage} |
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| 3 | \newcommand{\PSbox}[3]{\mbox{\rule{0in}{#3}\special{psfile=#1}\hspace{#2}}} |
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| 4 | \begin{document} |
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| 5 | \begin{enumerate} |
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| 6 | \item Helium diffusion through a pyrex tube |
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| 7 | \begin{center} |
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| 8 | \PSbox{tube.ps hoffset=-60 voffset=-5}{7.4in}{1.7in} |
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| 9 | \end{center} |
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| 10 | The diffusivity of helium in pyrex glass is vastly higher than that of any |
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| 11 | other gas. (Indeed, it is around 25 times larger than that of hydrogen, its |
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| 12 | closest competitor.) For this reason, it has been suggested that pyrex |
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| 13 | tubing be used as a filter to extract helium from natural gas. Here we will |
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| 14 | calculate the rate of helium production by diffusion through small pyrex |
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| 15 | tubes. |
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| 16 | |
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| 17 | \begin{enumerate} |
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| 18 | \item Write the differential equation for steady-state 1-D diffusion in the |
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| 19 | radial direction in cylindrical coordinates, and the general form of the |
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| 20 | solution. |
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| 21 | |
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| 22 | \item Write the solution for constant concentrations of helium on the inside |
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| 23 | and outside of the tube, {\em i.e.} $C_{\rm He, in}$ at the inner radius |
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| 24 | $R_{\rm in}$, and $C_{\rm He, out}$ at the outer radius $R_{\rm out}$. |
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| 25 | |
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| 26 | \item At 500$^\circ$ C, $D_{\rm He-pyrex}=2\times 10^{-8}\ \frac{\rm |
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| 27 | cm^2}{\rm s}$. Assuming the helium concentration in pyrex in equilibrium |
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| 28 | with a steady stream of natural gas/helium mixture $C_{\rm He, in}$ is |
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| 29 | 10$^{-5}$ $\rm\frac{g}{cm^3}$, and the helium concentration on the outside |
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| 30 | of the tubes $C_{\rm He, out}$ is 0, calculate the rate of helium |
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| 31 | extraction in a small tube array apparatus with 0.5 mm thick tubes with |
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| 32 | outer diameter of 2mm, and a total tube length of 10 meters (say, 100 tubes |
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| 33 | each 10 cm in length). Give the rate in cubic meters of helium at STP per |
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| 34 | hour. |
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| 35 | \end{enumerate} |
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| 36 | \end{enumerate} |
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| 37 | \end{document} |
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