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Natural vs artificial convection; heating curve

Short answer

Natural convection relies on density differences, giving low heat transfer; artificial convection uses fans/pumps for high coefficients and compact machines. The temperature rise-time curve is θ = θ_m (1 - e^{-t/τ}) + θ_i e^{-t/τ}, with θ_m = P/(Sλ) and τ = Gh/(Sλ).

Differentiate between natural and artificial convections in brief. Also derive an expression for the temperature rise-time curve for an electrical machine.

Convection is the transfer of heat from a hot surface by a moving fluid (air, hydrogen, oil). It is the main way heat leaves an electrical machine. Depending on what drives the fluid, it is called natural or artificial (forced) convection.

Natural vs artificial convection

PointNatural convectionArtificial (forced) convection
Fluid motion caused byDensity difference: hot fluid rises, cold fluid replaces itExternal agency: fan, blower or pump
Velocity of coolantLowHigh, controlled
Heat transfer coefficientLow (air about 10–15 W/m²°C)High; rises with air velocity, λ∝(1+0.1v)\lambda \propto (1 + 0.1v) roughly
Dependence on surface positionDepends on height and orientation of surfaceLittle dependence
Extra equipment and lossesNoneFans/pumps; extra cost and power loss
ReliabilityVery high; no moving partsDepends on fan/pump
Machine size for a ratingLargerSmaller (higher output per kg)
ExamplesSmall enclosed motors, ONAN transformersSelf- and separately-ventilated motors, ONAF/OFAF transformers, hydrogen-cooled alternators

The dissipation coefficient for forced air flow is often written λc=λc0(1+0.1 va)\lambda_c = \lambda_{c0}(1 + 0.1\,v_a), where vav_a is the air velocity in m/s. Doubling the cooling therefore lets a much larger loss be removed for the same rise.

Temperature rise–time curve of an electrical machine

Assumptions: the machine is a homogeneous body with uniform temperature; losses PP are constant; heat dissipated is proportional to the temperature rise.

Notation: GG = mass (kg), hh = specific heat (J/kg°C), SS = cooling surface (m²), λ\lambda = specific heat dissipation (W/m²°C), θ\theta = temperature rise at time tt.

In time dtdt, heat produced = heat stored + heat dissipated:

P dt=Gh dθ+Sλθ dtP\,dt = G h\,d\theta + S\lambda\theta\,dt dθdt+SλGhθ=PGh\begin{aligned} \frac{d\theta}{dt} + \frac{S\lambda}{Gh}\theta &= \frac{P}{Gh} \end{aligned}

Let θm=PSλ\theta_m = \dfrac{P}{S\lambda} (final steady rise) and τ=GhSλ\tau = \dfrac{Gh}{S\lambda} (heating time constant). The equation becomes

τdθdt+θ=θm\tau\frac{d\theta}{dt} + \theta = \theta_m

Separating variables and integrating from θi\theta_i at t=0t = 0:

∫θiθdθθm−θ=∫0tdtτln⁡θm−θiθm−θ=tτθ=θm(1−e−t/τ)+θi e−t/τ\begin{aligned} \int_{\theta_i}^{\theta}\frac{d\theta}{\theta_m - \theta} &= \int_0^t\frac{dt}{\tau} \\ \ln\frac{\theta_m - \theta_i}{\theta_m - \theta} &= \frac{t}{\tau} \\ \theta &= \theta_m\left(1 - e^{-t/\tau}\right) + \theta_i\,e^{-t/\tau} \end{aligned}

From cold: θ=θm(1−e−t/τ)\theta = \theta_m(1 - e^{-t/\tau}).

 rise
  ^      theta_m - - - - - - - - - - - - -
  |              ___....-------~~~~
  |         _.-''
  |      .-'   0.632 theta_m at t = tau
  |    /
  |  /
  | /
  +---|------|------|------|------> t
     tau    2tau   3tau   4tau

Cooling (losses removed): 0=Gh dθ+Sλcθ dt0 = Gh\,d\theta + S\lambda_c\theta\,dt, giving θ=θie−t/τc\theta = \theta_i e^{-t/\tau_c} with τc=Gh/(Sλc)\tau_c = Gh/(S\lambda_c).

Link between convection and the curve

  • Forced convection raises λ\lambda. This lowers both the final rise θm=P/(Sλ)\theta_m = P/(S\lambda) and the time constant τ=Gh/(Sλ)\tau = Gh/(S\lambda).
  • For the same permitted rise, a forced-cooled machine can carry larger losses, i.e. a higher output from the same frame.
  • In self-ventilated machines the fan stops at standstill, so λc<λ\lambda_c < \lambda and the cooling time constant is longer than the heating time constant.

✓ Answer checked by Claude Sonnet 5.5

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