| 1 | \documentclass{article} |
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| 2 | \usepackage{fullpage} |
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| 3 | \begin{document} |
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| 4 | \begin{enumerate} |
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| 5 | \item Heat conduction and diffusion in alloy casting |
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| 6 | |
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| 7 | In the die-casting of a relatively thick roughly plate-shaped metal alloy |
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| 8 | part, the liquid metal alloy cools and reaches a roughy uniform distribution |
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| 9 | at the melting point at time $t=0$, then solidifies with a plane front from |
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| 10 | the sides. The rate of solidification is limited by two types of heat |
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| 11 | transfer: conduction through the mold and to the environment can be |
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| 12 | represented by $q_x = h(T_s-T_{env})$ ($T_s$ is the outer surface metal |
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| 13 | temperature), and conduction through the already-solidified metal of |
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| 14 | thickness $Y$. |
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| 15 | |
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| 16 | \begin{enumerate} |
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| 17 | \item Sketch the temperature profile ($T$ vs. $x$, where $x$ is the distance |
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| 18 | from one side of the mold) across the solid metal shell and liquid metal |
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| 19 | interior for short times (small Bi) and long times (large Bi). |
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| 20 | |
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| 21 | \item Derive a simple expression for the growth rate $dY/dt$ which is valid |
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| 22 | for short times (small Bi). |
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| 23 | |
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| 24 | \item Derive a simple expression for the growth rate $dY/dt$ which is valid |
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| 25 | for long times. |
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| 26 | |
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| 27 | \item Sketch the relationship between solidified shell thickness $Y$ and time |
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| 28 | $t$, showing the transition from convection- to conduction-limited |
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| 29 | growth. |
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| 30 | \end{enumerate} |
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| 31 | |
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| 32 | As the metal solidifies, the lower solubility of the alloying element |
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| 33 | (solute) results in its ``rejection'' into the liquid. At steady-state, the |
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| 34 | concentration of the solute in the solid is that of the liquid $C_L$, but in |
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| 35 | the liquid at the liquid-solid interface, the concentration is much higher, |
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| 36 | say $5C_L$. |
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| 37 | |
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| 38 | \begin{enumerate} \setcounter{enumii}{4} |
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| 39 | \item Assuming that solidification front velocity $U$ is constant, that |
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| 40 | diffusion is slow enough that the diffusion boundary layer is much smaller |
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| 41 | than the part thickness, and that the effect of fluid flow is negligible, |
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| 42 | derive the steady-state general equation for concentration as a function of |
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| 43 | distance into the liquid from the moving interface $x'$ (that is, in the |
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| 44 | frame of reference of the moving interface). |
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| 45 | |
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| 46 | \item Fit this general solution to the boundary conditions in the liquid at |
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| 47 | $x'=0$ and $x'=\infty$ to give the particular concentration profile here. |
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| 48 | |
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| 49 | \item Approximately how thick is the solute-enriched layer in the liquid (an |
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| 50 | expression, not a number)? |
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| 51 | \end{enumerate} |
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| 52 | \end{enumerate} |
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| 53 | \end{document} |
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