This discussion focuses on calculating heat loss from a box surface into air, emphasizing the significance of convection types. The general equation for heat convection is defined as q = hAΔT, where h is the heat convection coefficient, A is the surface area, and ΔT is the temperature difference. The Nusselt Number (Nu) is introduced as a crucial factor in determining h, with specific equations provided for vertical and horizontal plates. Experimental results are suggested for estimating h, and coefficients for thermal conductivity, dynamic viscosity, and thermal diffusivity at various temperatures are included for practical application.
PREREQUISITES
Understanding of heat transfer principles, specifically convection.
Familiarity with the Nusselt Number and its significance in thermal analysis.
Knowledge of thermal conductivity, dynamic viscosity, and thermal diffusivity.
Basic grasp of fluid dynamics, particularly Rayleigh and Prandtl numbers.
NEXT STEPS
Research the calculation methods for the Nusselt Number in forced and free convection scenarios.
Explore the relationship between the Rayleigh Number and heat transfer in different geometries.
Study the impact of dynamic viscosity on heat transfer coefficients in various fluids.
Investigate experimental methods for determining the heat convection coefficient in real-world applications.
USEFUL FOR
Engineers, physicists, and thermal analysts involved in heat transfer calculations, particularly those working with convection in fluid dynamics and thermal management systems.
#1
nuby
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How can I calculate the heat loss from the surface area of a box into air?
Also, how can I calculate the heat/energy loss from a heated gas (into ambient air)?.
Consequently, if the box were in a forced convection flow region, it would probably be easier. If the air is stagnant, we have what's called Free Convection in that the air is moving due to the natural heating and cooling it experiences with proximity to the box.
Anyways, the general equation for heat convection is:
q = hA\Delta T
A is the area, dT is the difference in temperature, and q is the heat transfer. The only problem is h, the heat convection coefficient.
We will use experimental results to "guess" the value of h. We can relate the heat transfer coefficient to a non-dimensional number called the Nusselt Number:
\bar{Nu_L} = \frac{\bar{h}L}{k}
Where L is a characteristic length, k is the thermal conductivity, and h is the heat transfer coefficient that we want. We can get a relation for the Nusselt Number FOR A VERTICAL PLATE as:
\bar{Nu_L} = 0.68 + \frac{0.670 {Ra}^{1/4}_L}{\left[1+(0.492/Pr)^{9/16}\right]^{4/9}}
The Prandtl Number is easy enough to search for and fine the relation, its easy. The Raylaeigh (sp?) number is then given by:
Ra_L = \frac{g\beta(T_s - T_{\infty}L^3}{\nu\alpha}
Which has more easy material constants that you can look up.
For a horizontal plate, you can say that:
\bar{Nu_L}=0.54Ra^{1/4}_L \mbox{For 10^4<Ra_L<10^7}
and
\bar{Nu_L}=0.15Ra^{1/3}_L \mbox{For 10^7<Ra_L<10^11}
Then just add the effects all 5 sides together. Good luck,
Edit: Figured I'd give you some of those coefficients