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Distribution transformer efficiency and number of tubes

Short answer

Distribution transformers are designed for maximum all-day efficiency because they are energized 24 h with varying load; iron loss is constant, copper loss varies with load square. Placing maximum efficiency at 50–70% load reduces total energy losses. Required cooling tubes: n_t = (1/(8.8πd_t l_t))[(P_i+P_c)/θ – 12.5S_t] where d_t,l_t are tube diameter and length, S_t plain wall area, θ permissible oil temperature rise.

Why are distribution transformers designed to have maximum efficiency at loads much lower than full load? Derive the expression for calculating the number of tubes to be provided in a transformer tank.

Why maximum efficiency at less than full load

A distribution transformer stays energised for 24 hours but its load changes through the day and is often light (night hours). So the important figure is all-day (energy) efficiency:

ηall day=kWh output in 24 hkWh output+kWh losses in 24 h\eta_{all\ day} = \frac{\text{kWh output in 24 h}}{\text{kWh output} + \text{kWh losses in 24 h}}
  • Iron loss PiP_i occurs for all 24 hours, whatever the load.
  • Copper loss PcP_c occurs only in proportion to (load)², and is large only for a few peak hours.

Maximum efficiency occurs when copper loss = iron loss, i.e. at load fraction x=Pi/Pc,FLx = \sqrt{P_i/P_{c,FL}}. By keeping PiP_i small (lower BmB_m, good-quality steel) the maximum efficiency is placed at about 50–70% of full load, where the transformer runs most of the time. This minimises total energy loss in a day.

Number of cooling tubes

Let

  • Pi+PcP_i + P_c = total full-load loss (W)
  • StS_t = dissipating surface of plain tank walls (m²)
  • θ\theta = permissible mean temperature rise of oil (°C)

A plain tank wall dissipates by radiation ≈ 6 W/m²°C and by convection ≈ 6.5 W/m²°C, total 12.5 W/m²°C:

θ=Pi+Pc12.5 St\theta = \frac{P_i + P_c}{12.5\,S_t}

If this θ\theta is too high, tubes are added. Let the tube area be xStxS_t. Tubes do not add to radiation much (they screen each other), but they improve convection by about 35%:

6.5×1.35≈8.8 W/m2∘C6.5 \times 1.35 \approx 8.8\ \text{W/m}^2{}^\circ\text{C}

Heat dissipated with tubes:

Pi+Pc=θ[12.5 St+8.8 xSt]xSt=18.8(Pi+Pcθ−12.5 St)\begin{aligned} P_i + P_c &= \theta\left[12.5\,S_t + 8.8\,xS_t\right]\\ xS_t &= \frac{1}{8.8}\left(\frac{P_i + P_c}{\theta} - 12.5\,S_t\right) \end{aligned}

If each tube has diameter dtd_t and length ltl_t, its surface is πdtlt\pi d_tl_t, so

nt=xStπdtlt=18.8 πdtlt(Pi+Pcθ−12.5 St)n_t = \frac{xS_t}{\pi d_tl_t} = \frac{1}{8.8\,\pi d_tl_t}\left(\frac{P_i + P_c}{\theta} - 12.5\,S_t\right)

Round ntn_t up to the next whole number. Usually θ\theta = 35 °C (mean oil rise), tube diameter 50 mm and spacing 75 mm.

✓ Answer checked by Claude Sonnet 5.5

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