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Dimensionless numbers in convection

Short answer

Re = VL/ν (inertia/viscous), Pr = ν/α (momentum/thermal diffusivity), Nu = hL/k (convection/conduction), Gr = gβΔT L^3/ν^2 (buoyancy/viscous), St = h/(ρVc_p) (heat transferred/thermal capacity). Forced convection: Nu = f(Re,Pr); natural: Nu = f(Gr,Pr) with Ra = Gr Pr.

Define Reynolds, Prandtl, Nusselt, Grashof and Stanton numbers. State the physical significance of each and the relation between them in forced and natural convection.

Dimensionless numbers let results from one experiment be applied to similar situations of different size, fluid or velocity.

NumberDefinitionPhysical significance
Reynolds, ReReρVLμ=VLν\dfrac{\rho V L}{\mu} = \dfrac{VL}{\nu}Inertia force / viscous force. Decides laminar or turbulent flow
Prandtl, PrPrμcpk=να\dfrac{\mu c_p}{k} = \dfrac{\nu}{\alpha}Momentum diffusivity / thermal diffusivity. Fluid property; compares thickness of velocity and thermal layers
Nusselt, NuNuhLk\dfrac{hL}{k}Convection / conduction in the fluid layer of thickness LL; dimensionless heat transfer coefficient
Grashof, GrGrgβΔTL3ν2\dfrac{g\beta\Delta T L^3}{\nu^2}Buoyancy force / viscous force in natural convection
Stanton, StSthρVcp=NuRe Pr\dfrac{h}{\rho V c_p} = \dfrac{Nu}{Re\,Pr}Heat transferred to the fluid / thermal capacity of the flowing fluid

Relations

  • Forced convection: Nu=f(Re,Pr)Nu = f(Re, Pr), e.g. Nu=0.023 Re0.8Pr0.4Nu = 0.023\,Re^{0.8}Pr^{0.4} for turbulent flow in tubes.
  • Natural convection: Nu=f(Gr,Pr)Nu = f(Gr, Pr), usually written Nu=C (Gr Pr)mNu = C\,(Gr\,Pr)^m, where the product Gr PrGr\,Pr is the Rayleigh number RaRa.
  • Mixed convection: Gr/Re2Gr/Re^2 near 1 shows both effects are important.
  • St Pr2/3=f/2St\,Pr^{2/3} = f/2 is the Colburn analogy linking heat transfer with skin friction.

✓ Answer checked by Claude Sonnet 5.5

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