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06 / CHAPTER 11

Dimensionless thermal groups

Use Reynolds, Prandtl, and Nusselt numbers as regime clues.

Thermal Physics: original course diagram
A visual model for this course. Read it as a prompt for the assumptions behind the chapter.

ANCHOR EQUATION

Nusselt number

Nu=hLk

In symbols: Nu = hL/k

A dimensionless measure of convection relative to conduction.

Dimensionless groups compare competing mechanisms

A dimensionless number is a ratio of effects, not a decorative label. Reynolds compares inertia with viscosity; Prandtl compares momentum diffusion with thermal diffusion; Nusselt compares convection with conduction.

Cancel units to expose a regime

For flow speed U over length L, inertial stress scales as ρU² and viscous stress as μU/L. Their ratio is Re = ρUL/μ = UL/ν, where ν = μ/ρ. For heat transfer, Pr = ν/α compares momentum diffusivity ν with thermal diffusivity α; Nu = hL/k compares convective to conductive heat transfer.

Water at U = 1 m/s, L = 0.01 m, ρ = 1000 kg/m³, μ = 0.001 Pa·s has Re = 10,000. Inertia dominates viscosity at that scale, so laminar assumptions need evidence rather than habit.

A group predicts a tendency, not every detail

Transition thresholds depend on geometry and disturbances. Matching Re between a model nozzle and full-scale nozzle improves dynamic similarity, but surface roughness, gravity, and free-surface effects may introduce additional groups.

Work it: Calculate Re for water at U = 0.2 m/s in 2 mm and 20 mm tubes. Which is more likely to show inertial effects, and why does diameter change the result?