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Problems 403<br />

themselves at a reasonably steady temperature. Let the temperature in the ground be T(y, t),<br />

where у is the depth below the surface of the earth and t is the time, measured from the time<br />

of maximum temperature T o<br />

. Further, let the temperature far beneath the surface be T^, and<br />

let the surface temperature be given by<br />

7X0, t) - Т ж<br />

= 0 for t < 0<br />

T(0, t) - T x<br />

= (T o<br />

- T x<br />

) cos 0 (12C.5-1)<br />

Here (o = 2ir/t peT<br />

, in which t per<br />

is the time for one full cycle of the oscillating temperature—<br />

namely, 24 hours. Then it can be shown that the temperature at any depth is given by<br />

(12С.5-2)<br />

This equation is the heat conduction analog of Eq. 4D.1-1, which describes the response of the<br />

velocity profiles near an oscillating plate. The first term describes the "periodic steady state"<br />

and the second the "transient" behavior. Assume the following properties for the soil: 8 p =<br />

1515 kg/m 3 , к = 0.027 W/m • K, and C p<br />

= 800 J/kg • K.<br />

(a) Assume that the heating of the earth's surface is exactly sinusoidal, and find the amplitude<br />

of the temperature variation beneath the surface at a distance y. To do this, use only the<br />

periodic steady state term in Eq. 12C.5-2. Show that at a depth of 10 cm, this amplitude has<br />

the value of 0.0172.<br />

(b) Discuss the importance of the transient term in Eq. 12C.5-2. Estimate the size of this contribution.<br />

(c) Next consider an arbitrary formal expression for the daily surface temperature, given as a<br />

Fourier series of the form<br />

' ' °° = 2 (я„ cos ritot + b n<br />

sin ntot) (12C.5-3)<br />

i 0<br />

- 1 K n<br />

=0<br />

How many terms in this series are used to solve part (a)<br />

12C.6. Heat transfer in a falling non-Newtonian film. Repeat Problem 12B.4 for a polymeric fluid<br />

that is reasonably well described by the power law model of Eq. 8.3-3.<br />

12D.1. Unsteady-state heating of a slab (Laplace transform method).<br />

(a) Re-solve the problem in Example 12.1-2 by using the Laplace transform, and obtain the<br />

result in Eq. 12.1-31.<br />

(b) Note that the series in Eq. 12.1-31 does not converge rapidly at short times. By inverting<br />

the Laplace transform in a way different from that in (a), obtain a different series that is<br />

rapidly convergent for small times. 9<br />

(c) Show how the first term in the series in (b) is related to the "short contact time" solution<br />

of Example 12.1-1.<br />

12D.2. The Graetz-Nusselt problem (Table 12D.2).<br />

(a) A fluid (Newtonian or generalized Newtonian) is in laminar flow in a circular tube of radius<br />

R. In the inlet region z < 0, the fluid temperature is uniform at T v<br />

In the region z > 0, the<br />

wall temperature is maintained at T o<br />

. Assume that all physical properties are constant and<br />

8<br />

W. M. Rohsenow, J. P. Hartnett, and Y. I. Cho, eds., Handbook of Heat Transfer, 3rd edition,<br />

McGraw-Hill (1998), p. 2.68.<br />

9<br />

H. S. Carslaw and J. C. Jaeger, Conduction of Heat in Solids, 2nd edition, Oxford University Press<br />

(1959), pp. 308-310.

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