Start with your question

Why visitors arrive: You need a quick lookup for Reynolds, Mach, Nusselt, or similarity checklists.

Your question: Which dimensionless groups apply to my flow or heat-transfer problem?

You may also be asking

  • Where is the full dimensional analysis lesson?
  • How do I get fluid properties?
  • How are groups used in experiments?

Where to go next

Dimensionless groups reference

A durable lookup for the scaling groups that appear across fluid mechanics, heat transfer, and aerothermal experiments — with definitions, typical use, and pointers to the full derivations in the fluid mechanics curriculum.

Reference Similarity Fluid mechanics Heat transfer

When to reach for a Pi group

Dimensionless numbers compress competing physical effects into ratios. They are how wind-tunnel tests claim relevance to engine conditions, how probe calibrations are transferred between facilities, and how low-order heat-exchanger models stay traceable.

Fluid mechanics

Group Definition Physical meaning Typical use
Reynolds Re \(\mathrm{Re} = \dfrac{\rho U L}{\mu}\) Inertia ÷ viscous forces Laminar/turbulent transition; dynamic similarity in pipe and external flows; probe calibration transfer
Mach Ma \(\mathrm{Ma} = \dfrac{U}{a}\) Flow speed ÷ sound speed Compressibility; choking; high-speed tunnel matching
Froude Fr \(\mathrm{Fr} = \dfrac{U}{\sqrt{g L}}\) Inertia ÷ gravity Free-surface flows; wave phenomena
Weber We \(\mathrm{We} = \dfrac{\rho U^2 L}{\sigma}\) Inertia ÷ surface tension Jet breakup; capillary-dominated flows
Stokes St \(\mathrm{St} = \dfrac{\mu U}{\rho g D^2}\) (form varies) Viscous ÷ gravitational effects on particles Particle settling; related to Fr/Re ratios — see curriculum problem set
Euler Eu \(\mathrm{Eu} = \dfrac{\Delta p}{\rho U^2}\) Pressure forces ÷ inertia Cavitation; pressure-loss coefficients in internal flows

Heat transfer

Group Definition Physical meaning Typical use
Nusselt Nu \(\mathrm{Nu} = \dfrac{h L}{k}\) Convective ÷ conductive transport at a wall Convective HTC correlations; heat-exchanger segment sizing
Prandtl Pr \(\mathrm{Pr} = \dfrac{c_p \mu}{k} = \dfrac{\nu}{\alpha}\) Momentum diffusivity ÷ thermal diffusivity Coupling velocity and thermal boundary layers; property evaluation from air properties
Péclet Pe \(\mathrm{Pe} = \mathrm{Re}\,\mathrm{Pr}\) Advection ÷ diffusion of energy Thermal entrance lengths; conjugate problems
Biot Bi \(\mathrm{Bi} = \dfrac{h L}{k_{\mathrm{solid}}}\) External convection ÷ internal conduction in a solid Lumped-capacitance validity; transient thermography interpretation — see HPT thermography note
Stanton St \(\mathrm{St} = \dfrac{h}{\rho U c_p}\) Heat transfer ÷ enthalpy flux Boundary-layer heat transfer; Reynolds analogy contexts

Similarity checklist for experiments

Before claiming a model test represents a prototype, state which Pi groups are matched and which are relaxed — and document the consequence in the uncertainty budget.

Test type Usually matched Often relaxed Read next
Incompressible internal flow Re, geometry (scale) Absolute pressure if density weakly varying Viscous flow module
High-speed external aerodynamics Re, Ma, γ (gas) Wall temperature if adiabatic assumption holds CFD–experiment validation
Convective heat transfer Re, Pr, boundary-layer state Bi in the solid if lumped model justified Thermal & additive design
Pneumatic probe calibration Re at calibration point, Mach regime Facility-specific polynomial bias — see probe uncertainty note Instrumentation theme

About this work

Lucas Rey — Aerothermal systems engineer and academic tutor.

  • University of Oxford: DPhil Researcher, Thermofluids Institute.
  • University of Cambridge: Alumnus.
  • Rolls-Royce: Sponsored researcher (High-pressure turbine programme).

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