| 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 New tundish design\footnote{This problem was inspired by Robert Hyers |
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| 7 | (now on the faculty at the University of Massachusetts at Amherst), and the |
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| 8 | design shown here is informally known as the ``Hyers Tundish''.} |
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| 9 | |
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| 10 | A tundish is a bathtub-shaped vessel which holds liquid steel between the |
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| 11 | ladle and continuous caster. It is used to float ceramic inclusion particles |
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| 12 | out of liquid steel, and maintain a constant liquid level and head of |
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| 13 | pressure above the continuous caster, providing a steady flow rate and |
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| 14 | velocity of metal into the caster. |
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| 15 | |
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| 16 | A new design for tundishes has been proposed which uses vertical plates of |
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| 17 | refractory ceramics to separate the flow into several channels, as shown |
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| 18 | below. |
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| 19 | \begin{center} |
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| 20 | \PSbox{newtun.ps}{5in}{2.5in} |
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| 21 | \end{center} |
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| 22 | Data: |
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| 23 | \begin{itemize} |
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| 24 | \item Steel $\rm\rho=7000\frac{kg}{m^3}$, $\rm\eta=5.2\times10^{-3}\frac{kg} |
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| 25 | {m\cdot s}$; typical ceramic particle $\rm\rho=3700\frac{g}{cm^3}$ |
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| 26 | \item Tundish dimensions: $H=1$m, $L=1.5$m, $W_c=0.15$m, $W=1$m |
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| 27 | \item Flow rate: $Q=2\frac{\rm liters}{\rm sec}$ (=0.002$\rm\frac{m^3}{s}$) |
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| 28 | \end{itemize} |
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| 29 | |
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| 30 | \begin{enumerate} |
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| 31 | \item \label{uav} Using the flow rate $Q$ given above, and assuming that flow |
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| 32 | is distributed equally to each of the four vertical channels, calculate the |
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| 33 | average velocity of molten steel through those channels. |
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| 34 | |
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| 35 | \item Assuming flow is fully-developed, what is the Reynolds number of the |
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| 36 | metal flow in the channels? What would the Reynolds |
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| 37 | number be without the vertical plates between the channels (that is, one |
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| 38 | big open box)? Will the flow likely be laminar in each situation (with and |
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| 39 | without the plates)? |
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| 40 | |
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| 41 | \item \label{maxu} Treating a channel as a pair of parallel plates with |
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| 42 | fully-developed steady-state laminar flow between them, calculate the |
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| 43 | maximum velocity of molten metal in a channel. |
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| 44 | |
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| 45 | \item Consider a ceramic particle which enters a channel at the bottom center |
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| 46 | and rises through the molten steel as it is being carried forward by the |
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| 47 | flow of metal in the center of the channel. Its $y$-direction velocity is |
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| 48 | the maximum velocity of the fluid (since it is in the center of the |
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| 49 | channel), and its $z$-direction velocity is its upward terminal velocity. |
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| 50 | What is the minimum upward terminal velocity this particle can have and |
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| 51 | still reach the top before it gets to the end of the channel? (If you |
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| 52 | didn't get an answer to part \ref{maxu}, use your value from part \ref{uav} |
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| 53 | as the molten steel flow velocity in the center.) |
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| 54 | |
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| 55 | \item What is the spherical particle size corresponding to this terminal |
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| 56 | velocity? (If you assume Stokes flow around the particle, be sure to check |
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| 57 | it!) |
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| 58 | |
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| 59 | \item Calculate the entrance length for flow in these channels. What does |
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| 60 | this tell you about the validity of our assumptions above? |
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| 61 | |
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| 62 | \item Considering only the faces of the plates (not the ends), and assuming |
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| 63 | uniform velocity at the entrances of the channels, estimate the drag force |
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| 64 | on a single plate. |
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| 65 | \end{enumerate} |
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| 66 | \end{enumerate} |
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| 67 | \end{document} |
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