root/trunk/matml/transport/problems/castdiffheat/castdiffheat.tex

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New problem: Heat conduction and diffusion in alloy casting

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