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For cable modelling, we typically assume constant thermal conductivity, see Thermal Analysis.
To consider the effect of convection (natural or forced in a gas or liquid), Newton's law of cooling is used:
$q=hA\left(T-{T}_{a}\right)$
for air (a common cable installation medium), the convection heat transfer coefficient h, flowing at velocity v, can be obtained from:
$h=7.371+6.43{v}^{0.75}$
To set a convection boundary conditions, we can use a Neumann condition with q = desired convection coefficient and g = temperature of environment times the convection coefficient.
Convection is a complex topic, requiring a detailed understanding of heat flow, fluid flow and the behaviour of gases as they flow across surfaces. For cable sizing, to achieve this level of technical detail is not practical nor achievable in many situations. One effective technique when solving equations for enclosed spaces is the use of an effective thermal conductivity, k_{e}. Using an effective thermal conductivity enables the air to be treated from a conduction view, eliminating much of the complexity in implements full connectivity solutions.
For an enclosed spaced, the effective thermal conductivity is given by:
${k}_{e}=k{N}_{u}$
The Grashof number is given by:
${G}_{r\delta}=\frac{g\beta \left({T}_{1}-{T}_{2}\right){\delta}^{3}}{{\nu}^{2}}$
with: $\beta =\frac{1}{{T}_{f}}$ and ${T}_{f}=\frac{{T}_{1}+{T}_{2}}{2}$
Note: T_{f} is in Kelvin (not °C).
Experimental results for free convection in an enclosure give:
${N}_{{u}_{\delta}}=C{\left({G}_{{r}_{\delta}}{P}_{r}\right)}^{n}{\left(\frac{L}{\delta}\right)}^{m}$
Typically we can take g = 9.80665 and for air:
Note: δ is the hydro-dynamic boundary layer thickness.
Values of C, n and m can be obtained from the following table using the Grashof-Prandtl number product:
A - area, m^{2} g - acceleration of gravity, m/s^{2} h - convection heat transfer coefficient, W/m^{2}.°C k - thermal conductivity, W/m.°C k_{e} - effective thermal conductivity, W/m.°C T, T_{1}, T_{2}, T_{a} - temperature, K v - velocity of air, m/s ν - kinematic viscosity, m^{2}/s
q - heat flow, W (or Joules/second) $\dot{q}$ - heat generated per unit volume, W/m^{3}
β - coefficient of thermal expansion δ - enclosure dimension, m
G_{r} - Grashof number N_{u} - Nusselt number P_{r} - Prandtl number R_{a} - Rayleigh number