Question 3.17: Electrical heaters are used in contact heating (i.e., conduc...

Electrical heaters are used in contact heating (i.e., conduction heating) for various thermal processes. A common example is the fabric iron, rendered in Figures (a) and (b). A large fraction of the electrical power flowing into the iron, flows into the fabric. This is designated as Q_{s}. The contact area is A_{k} . Then the heat flux is q_{s} = Q_{s}/A_{k} . Consider a relatively thick fabric that is initially at T_{i} . Here thick indicates that we are interested in elapsed times such that the effect of heating at the surface (designated by x = 0) has not yet penetrated to the other side of the fabric.
The fabric has thermal diffusivity \left\langle \alpha \right\rangle =\left\langle k\right\rangle /\left\langle\rho c_{p}\right\rangle = 10^{−7} m^{2}/s , and \left\langle k\right\rangle = 0.2 W/m-K . The heat flux is q_{s} = −2 × 10^{4} W/m^{2} , and the initial temperature is T (t = 0) = 20^{\circ }C . The elapsed time is t = 30 s. The surface temperature may exceed the charring (or scorching) temperature of fabric Tc = 180^{\circ }C , and then permanent damage is caused to the fabric.

(a) Determine the surface temperature T_{s}(t) = T (x = 0, t = 30 s).
(b) Determine the temperature at location x = 3 mm from the surface, for this elapsed time, i.e., T (x = 3 mm, t = 30 s).

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Because of the thick-layer assumption, the semi-infinite slab geometry can be used. The solution for the transient temperature distribution is given in Table  and the magnitude of the error function is listed in Table. The transient temperature distribution is given in Table as

T (x, t) = T (t = 0) −\frac{q_{s}(4\left\langle \alpha \right\rangle t/\pi )^{1/2}}{\left\langle k\right\rangle } e^{-x^{2}/(4\left\langle\alpha \right\rangle t )}+\frac{q_{s}x}{\left\langle k\right\rangle } \left\{1-erf\left[\frac{x}{2(\left\langle\alpha \right\rangle t)^{1/2}} \right] \right\}

(a) For x = 0 and t = 30 s, we have

T(x=0,t)=T_{t}(t)=T (t = 0) −\frac{2q_{s}(\left\langle \alpha \right\rangle t/\pi )^{1/2}}{\left\langle k\right\rangle }

This shows that the surface temperature changes with q_{s} to the first power and t to the 1/2 power.
Using the numerical values, we have

  T (x = 0, t = 30 s)

 

= 20(^{\circ }C) −\frac{2\times [-(2\times 10^{4})(W/m^{2})][10^{-7}(m^{2}/s)\times 30(s)/\pi ]^{1/2}}{0.2(W/m-^{\circ }C)}

 

=20(^{\circ }C)+195.5(^{\circ }C)=215.5^{\circ }C

This shows that the surface temperature exceeds the charring temperature at an elapsed time of t = 30 s.
(b) For x = 3 mm and at t = 30 s, we have

\frac{x^{2}}{4\left\langle \alpha \right\rangle t}=\frac{(3\times 10^{-3})^{2}(m^{2})}{4\times 10^{-7}(m^{2}/s)\times 30(s)} =0.75

 

erf[(0.75)^{1/2}]=erf(0.8660)=0.7850        from Figure (a)(i) or for more accurate results from interpolation in Table

T (x = 3mm, t = 30 s)= 20(^{\circ }C) −\frac{2\times [-(2\times 10^{4})(W/m^{2})][10^{-7}(m^{2}/s)\times 30(s)/\pi ]^{1/2}}{0.2(W/m-^{\circ }C)}e^{-0.75}

 

+\frac{[-2\times 10^{4}(W/m^{2})]\times 3\times 10^{-3}(m)}{0.2(W/m-^{\circ }C)}[1-erf(0.8660)]

 

= 20(^{\circ }C)+92.34(^{\circ }C)-64.49(^{\circ }C)=47.85^{\circ }C
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