Heat Loss Through a Short Cylinder

AI Thread Summary
The discussion focuses on estimating the cooling time and heat transfer for a short metal cylinder exposed to room temperature. The cylinder, with a diameter and height of 145 mm, initially at 1045 K, cools to 600 K, with calculations indicating a time of approximately 4115 seconds. The heat loss is influenced by both convection and conduction, necessitating the inclusion of all surface areas in the calculations. The complexity arises from the transient nature of heat conduction, where temperature distribution is not uniform. A solution may require either analytical methods for partial differential equations or approximations using dimensionless graphs.
Reefy
Messages
62
Reaction score
1

Homework Statement


A short metal cylinder 145 mm in diameter and 145 mm high at 1045 K
is suddenly exposed (all sides exposed) to a room air temperature at
300 K with h=25 W/m².K. Assume that for the metal k=40W/m.K, den=7800 kg/m3
and Cp=c=600 J/kg.K. Estimate (a) the time required for the cylinder to
cool down to 600K at center and heat transferred.

Homework Equations



$$V = \frac {πD^2L} {4}$$

$$A_s = \frac {πD^2} {2} + πDL$$

$$Bi = \frac {hV}{kA}$$

$$\frac {T_o - T_∞}{T_i - T_∞} = e^{ \frac {htA_s} {ρVc}} $$

$$Q_conduction = -kA\frac{dT}{dr}$$

$$Q_convection = hA_exposed (T_s - T_∞)$$

The Attempt at a Solution


[/B]
$$ t = \frac {ρVc}{hA_s} [ln {\frac {T_o - T_∞}{T_i - T_∞}}]$$

t ≈ 4115s

Where T = 300 K, To = 600 K, Ti = 1045 K

My main issue is determing the heat loss transferred. From my understanding, a short cylinder means that we can't assume the top and bottom areas are negligible in determining heat loss so they have to be factored in. But I can't figure out equation setup for total heat loss. I'm almost positive that heat loss is by convection AND conduction and when we combine the two, we multiply it by the time to determine the heat loss in Joules.
 
Physics news on Phys.org
This is a transient heat conduction problem in which the temperature within the cylinder is not uniform during the transition (distributed parameter system). If you don't have any dimensionless graphs of solutions to this problem, you are going to have to solve the partial differential equations analytically, or figure out a clever way of approximating the solution from graphs for other dimensionless solutions.
 
Back
Top