Base dimensions W = D = 100 mm, fin thickness t = 2 mm, base-to-ambient temperature difference ΔT = 50 K are assumed.
Left: side view with N fins standing on the base / Right: tanh(x)/x fin efficiency curve (yellow dot = current m·Lc)
Fin parameter for a straight rectangular fin (thin-fin, adiabatic-tip approximation). h = convection coefficient, k = fin conductivity, t = fin thickness:
$$m = \sqrt{\frac{2h}{k\,t}}$$Fin efficiency. Lc = L + t/2 is the corrected fin length:
$$\eta_f = \frac{\tanh(m\,L_c)}{m\,L_c}$$Overall surface efficiency. N = number of fins, A_f = single-fin area, A_total = N·A_f + (A_b − N·t·D):
$$\eta_o = 1 - \frac{N\,A_f}{A_\text{total}}(1 - \eta_f)$$Total heat transfer. T_b = base temperature, T_∞ = ambient:
$$Q = \eta_o\,h\,A_\text{total}\,(T_b - T_\infty)$$The smaller m·Lc (large k, short L), the closer the fin efficiency is to 1. Increasing N grows A_total and Q, but real designs must also account for the airflow penalty.