Reynolds analogy

Short description: Analogy in fluid dynamics

The Reynolds Analogy is popularly known to relate turbulent momentum and heat transfer.[1] That is because in a turbulent flow (in a pipe or in a boundary layer) the transport of momentum and the transport of heat largely depends on the same turbulent eddies: the velocity and the temperature profiles have the same shape.

The main assumption is that heat flux q/A in a turbulent system is analogous to momentum flux τ, which suggests that the ratio τ/(q/A) must be constant for all radial positions.

The complete Reynolds analogy* is:

The complete Reynolds analogy is:

f2=hcpG=k'cvavg

where:

* f is the Fanning friction factor;
* h is the heat transfer coefficient;
* cp is the specific heat at constant pressure;
* G is the mass velocity (mass flow rate per unit area).

Experimental data for gas streams agree approximately with above equation if the Schmidt and Prandtl numbers are near 1.0 and only skin friction is present in flow past a flat plate or inside a pipe. When liquids are present and/or form drag is present, the analogy is conventionally known to be invalid.[1]

In 2008, the qualitative validity of Reynolds' analogy was re-visited for laminar flow of an incompressible fluid with variable dynamic viscosity (μ).[2] It was shown that the inverse dependence of Reynolds number (Re) and skin friction coefficient (cf) is the basis for the validity of the analogy in both constant and variable μ flows.

For μ=const., the analogy reduces to the popular form where the Stanton number (St) increases with increasing Re. For variable μ, it reduces to St increasing with decreasing Re. Consequently, the Chilton–Colburn analogy is qualitatively valid whenever the Reynolds' analogy is valid. Furthermore, the validity of the analogy is linked to the applicability of Prigogine's Theorem of Minimum Entropy Production.[3] Thus, Reynolds' analogy is valid for flows that are close to being fully developed, where changes in the gradients of velocity and temperature along the flow are small.[2]

## See also

* Reynolds number
* Chilton and Colburn J-factor analogy

## References

1. ↑ 1.0 1.1 Geankoplis, C.J. Transport processes and separation process principles (2003), Fourth Edition, p. 475.
2. ↑ 2.0 2.1 Mahulikar, S.P., & Herwig, H., 'Fluid friction in incompressible laminar convection: Reynolds' analogy revisited for variable fluid properties,' European Physical Journal B: Condensed Matter & Complex Systems, 62(1), (2008), pp. 77-86.
3. ↑ Prigogine, I. Introduction to Thermodynamics of Irreversible Processes (1961), Interscience Publishers, New York.

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