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| Teaching Since: | May 2017 |
| Last Sign in: | 399 Weeks Ago |
| Questions Answered: | 66690 |
| Tutorials Posted: | 66688 |
MCS,PHD
Argosy University/ Phoniex University/
Nov-2005 - Oct-2011
Professor
Phoniex University
Oct-2001 - Nov-2016
1.63   A 50 mm X 45 mm X 20 mm cell phone  charger has a surface temperature of Ts = 33°C when plugged into an electrical wall outlet but not in use. The surface of the charger is of emissivity s = 0.92 and is subject to a free convection heat transfer coefficient of h = 4.5 W/m2 · K. The room air and wall tempera- tures are T00 = 22°C and Tsur = 20°C, respectively. If electricity costs C = $0.18/kW · h, determine the
daily cost of leaving the charger plugged in when not in use.
ri = 0.5 m
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(a)Â Â Â Assuming negligible temperature gradients in the canister wall and a constant heat flux qi", develop an equation that governs the variation of the wall tem- perature with time during the transient process. What is the initial rate of change of the wall tem- perature if q"i = 105 W/m2?
(b)Â Â What is the steady-state temperature of the wall?
(c)Â Â Â
The convection coefficient depends on the velocity associated with fluid flow over the canister and whether the wall temperature is large enough to induce boiling in the liquid. Compute and plot the steady-state temperature as a function of h for the range 100 h 10,000 W/m2 · K. Is there a value of h below which operation would be unacceptable?
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