| 1 | \documentclass{article} |
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| 2 | \usepackage{fullpage,lmodern} |
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| 3 | \usepackage[T1]{fontenc} |
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| 4 | \begin{document} |
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| 5 | \begin{enumerate} |
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| 6 | \item Freezing Lake |
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| 7 | \begin{enumerate} |
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| 8 | \item This was a straightforward application of finite difference principles: |
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| 9 | \begin{eqnarray} |
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| 10 | \label{eq:energydifference} |
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| 11 | \frac{H_{i,n+1}-H_{i,n}}{\Delta t} &=& |
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| 12 | \frac{\left[k\frac{\partial T}{\partial x}\right]_{i+\frac{1}{2},n} - |
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| 13 | \left[k\frac{\partial T}{\partial x}\right]_{i-\frac{1}{2},n}}{\Delta x} \\ |
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| 14 | \nonumber &=& \frac{k_{i+\frac{1}{2},n}(T_{i+1,n}-T_{i,n}) - |
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| 15 | k_{i-\frac{1}{2},n}(T_{i,n}-T_{i-1,n})}{(\Delta x)^2} |
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| 16 | \end{eqnarray} |
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| 17 | |
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| 18 | \item At the bottom of the lake, the flux at $x_{i+\frac{1}{2}}$ is zero, so |
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| 19 | we remove it from equation \ref{eq:energydifference}: |
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| 20 | \begin{equation} |
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| 21 | \label{eq:bottombound} |
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| 22 | \frac{H_{i,n+1}-H_{i,n}}{\Delta t} = |
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| 23 | \frac{k_{i+\frac{1}{2},n}(T_{i+1,n}-T_{i,n})}{(\Delta x)^2}. |
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| 24 | \end{equation} |
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| 25 | At the top of the lake, the flux is given by $h(T_{air}-T)$, so we replace |
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| 26 | the $i+\frac{1}{2}$ part of the equation. But we have to be careful with |
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| 27 | the $\Delta x$es, distinguishing between the one used for the divergence of |
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| 28 | the flux, and that used to calculate the flux itself at |
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| 29 | $x_{i-\frac{1}{2}}$: |
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| 30 | \begin{equation} |
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| 31 | \label{eq:topbound} |
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| 32 | \frac{H_{i,n+1}-H_{i,n}}{\Delta t} = \frac{h(T_{air}-T_{i,n}) - |
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| 33 | \frac{k_{i-\frac{1}{2},n}(T_{i,n}-T_{i-1,n})}{\Delta x}}{\Delta x}. |
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| 34 | \end{equation} |
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| 35 | |
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| 36 | \item \label{timestep} First, extend the properties table in the problem to |
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| 37 | include thermal diffusivity and stable timestep (for $\Delta x=0.01$m): |
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| 38 | \begin{center} |
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| 39 | \begin{tabular}{l|c|c|} |
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| 40 | Material & Liq. water & Sol. water \\ \hline |
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| 41 | Conductivity $k$, $\rm\frac{W}{m\cdot K}$ & 0.56 & 2.3 \\ |
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| 42 | Heat capacity $c_p$, $\rm\frac{J}{kg\cdot K}$ & 4200 & 2100 \\ |
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| 43 | Density $\rho$, $\rm\frac{kg}{m^3}$ & 1000 & 920 \\ \hline |
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| 44 | Thermal diffusivity $\alpha$, $\rm\frac{m^2}{s}$ & $1.33\times10^{-7}$& |
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| 45 | $1.19\times10^{-6}$ \\ |
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| 46 | Stability criterion, sec& $\Delta t\leq375$& $\Delta t\leq42$ \\ \hline |
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| 47 | \end{tabular} |
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| 48 | \end{center} |
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| 49 | If we use the liquid water criterion, the liquid is stable but the solid |
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| 50 | clearly is not. So we use the smaller timestep criterion (solid water, 42 |
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| 51 | seconds), which corresponds to the larger thermal diffusivity. |
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| 52 | |
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| 53 | \item \label{timescales} The three timescales: |
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| 54 | \begin{enumerate} |
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| 55 | \item \label{condtime} For $L=0.1$m, the time required to reach |
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| 56 | steady-state in liquid water is given by $t\sim L^2/\alpha = 75,000$ |
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| 57 | seconds (about 20 hours). |
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| 58 | \item \label{condlimit} First we solve the differential equation: |
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| 59 | \begin{equation} |
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| 60 | \label{eq:condeqn} |
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| 61 | \rho\Delta H_f\frac{dX}{dt} = k\frac{\Delta T}{X} |
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| 62 | \end{equation} |
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| 63 | $$X dX = \frac{k\Delta T}{\rho\Delta H_f} dt$$ |
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| 64 | $$\frac{X^2}{2} = \frac{k\Delta T}{\rho\Delta H_f} t + const$$ |
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| 65 | For $X=0$ at $t=0$, the integration constant is zero, so the time is |
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| 66 | given by |
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| 67 | \begin{equation} |
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| 68 | \label{eq:condresult} |
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| 69 | t = \frac{\rho\Delta H_f X^2}{2k\Delta T} = |
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| 70 | \frac{\rm 920\frac{kg}{m^3}\cdot334,000\frac{J}{kg}\cdot(0.1m)^2} |
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| 71 | {\rm 2\cdot2.3\frac{J}{s\cdot m\cdot K}\cdot10K} = 66,800{\rm s}. |
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| 72 | \end{equation} |
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| 73 | \item \label{convlimit} The differential equation for convection-limited |
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| 74 | freezing is even simpler: |
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| 75 | \begin{equation} |
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| 76 | \label{eq:conveqn} |
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| 77 | \rho\Delta H_f\frac{dX}{dt} = h\Delta T |
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| 78 | \end{equation} |
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| 79 | $$\rho\Delta H_f X = h\Delta T t + const.$$ |
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| 80 | Again the integration constant is zero, so using $h=10\frac{W}{m^2\cdot |
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| 81 | K}$ (from part \ref{fdsolution}), required time is given by: |
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| 82 | \begin{equation} |
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| 83 | \label{eq:convresult} |
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| 84 | t = \frac{\rho\Delta H_f X}{h\Delta T} = |
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| 85 | \frac{\rm 920\frac{kg}{m^3}\cdot334,000\frac{J}{kg}\cdot0.1m} |
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| 86 | {\rm 10\frac{W}{m^2\cdot K}\cdot10K} = 307,280{\rm s}. |
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| 87 | \end{equation} |
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| 88 | This is clearly the dominant timescale in this problem. |
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| 89 | \end{enumerate} |
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| 90 | We can add the above results to give a rough estimate of the total time |
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| 91 | required to freeze the lake, which gives us 449,000 seconds, or about 5 |
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| 92 | days. At 42 seconds/timestep (from part \ref{timestep}), this will require |
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| 93 | about ten thousand timesteps (!). |
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| 94 | |
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| 95 | \item \label{fdsolution} The spreadsheet provided implements the above |
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| 96 | equations and boundary conditions. Two plots are provided: one giving the |
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| 97 | information requested in the asignment, and the other with plots at a few |
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| 98 | more times in between. Times for each set of plots are as follows: |
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| 99 | |
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| 100 | \begin{center} |
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| 101 | \begin{tabular}{|lcc||lcc|} |
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| 102 | Time & Plot 1 series \# & Plot 2 series \# & |
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| 103 | Time & Plot 1 series \# & Plot 2 series \# \\ \hline |
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| 104 | 0 & 1 & 1 & 158634 & & 8 \\ |
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| 105 | 3360 & & 2 & 204414 & 3 & 9 \\ |
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| 106 | 6846 & & 3 & 251034 & & 10 \\ |
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| 107 | 10080 & & 4 & 301434 & & 11 \\ |
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| 108 | 13760 & 2 & 5 & 351834 & & 12 \\ |
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| 109 | 62034 & & 6 & 402234 & & 13 \\ |
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| 110 | 110334 & & 7 & 448560 & 4 & 14 \\ \hline |
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| 111 | \end{tabular} |
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| 112 | \end{center} |
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| 113 | |
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| 114 | Note that the calculated total time of freezing is within 0.2\% of the |
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| 115 | estimate in part \ref{timescales}. |
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| 116 | \end{enumerate} |
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| 117 | \newpage |
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| 118 | \begin{center} |
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| 119 | \pdfimageresolution 180 |
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| 120 | $\ $\pdfximage{plot1.png}\pdfrefximage\pdflastximage$\ $ |
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| 121 | |
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| 122 | $\ $\pdfximage{plot2.png}\pdfrefximage\pdflastximage$\ $ |
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| 123 | \end{center} |
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| 124 | \end{enumerate} |
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| 125 | \end{document} |
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| 126 | |
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| 127 | |
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| 128 | |
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