Reference: J.P. Holman, "Heat Transfer", 7th ed., 1990, McGraw-Hill, p. 181-183.
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A 0.01 by 0.02 m. ceramic strip is initially at a uniform temperature of 300oC.
The left and right sides are maintained at a constant temperature of 300oC.
The bottom surface is perfectly insulated. Assume unit depth for this part.
Radiation is not to be considered in this problem.
| The properties of the ceramic are: | The top surface is exposed to a convection environment: |
| thermal conductivity of 3.0 W/m-oC | h = 200 W/m2-oC |
| density of 1600 kg/m3 | TBULK = 50oC |
| specific heat of 800 J/kg-oC |
Model this cooling process for 12 seconds.
MAKE SURE that the air temperature (TBULK) is at 50oC for the ENTIRE simulation.
Find the temperature at the three points (A, B, and C) labeled on the figure as the part cools.
Compute the average rate of
heat loss (in Watts) over
the 12 second process.
In the time history postprocessor, you could simply average the
"instantaneous" value of heat flow rate at each solution - OR - more
accurately, you could integrate the heat loss rate over the time interval and
finally divide by the time period to obtain the average heat loss rate.
Turn in:
Reminder: All project reports will be typed, and include:
** from the textbook: The average rate of heat loss over 12 sec. = 464.4 W
| time (sec.) | Ta | Tb | Tc |
| 0 | 300 | 300 | 300 |
| 2 | 268.75 | 300 | 300 |
| 4 | 253.13 | 294.14 | 300 |
| 6 | 245.31 | 287.55 | 297.80 |
| 8 | 239.48 | 282.38 | 293.96 |
| 10 | 235.35 | 277.79 | 290.08 |
| 12 | 231.97 | 273.95 | 286.32 |