In continuum mechanics, the Péclet number (Pe, after Jean Claude Eugène Péclet) is a class of dimensionless numbers relevant in the study of transport phenomena in a continuous environment. It is defined to be the ratio of the rate of advection of a physical quantity by the flow to the rate of diffusion of the same quantity driven by an appropriate gradient. In the context of species or mass transfer, the Péclet number is the product of the Reynolds number and the Schmidt number (Re × Sc). In the context of the thermal fluids, the thermal Péclet number is equivalent to the product of the Reynolds number and the Prandtl number (Re × Pr).

Definition

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Plan view: For , advection is negligible, and diffusion dominates mass transport.

The Péclet number is defined as

Plan view: For , diffusion and advection occur over equal times, and both have a non-negligible influence on mass transport.

Usages

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Mass transfer

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For mass transfer, it is defined as

where L is the characteristic length, u the local flow velocity, D the mass diffusion coefficient, Re the Reynolds number, Sc the Schmidt number.

Such ratio can also be re-written in terms of times, as a ratio between the characteristic temporal intervals of the system:

For the diffusion happens in a much longer time compared to the advection, and therefore the latter of the two phenomena predominates in the mass transport.

Heat transfer

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Plan view: For , diffusion is negligible, and advection dominates mass transport.

For heat transfer, the Péclet number is defined as where Pr the Prandtl number, and α the thermal diffusivity, where k is the thermal conductivity, ρ the density, and cp the specific heat capacity.

Engineering applications

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In engineering applications, the Péclet number is often very large. In such situations, the dependency of the flow upon downstream locations is diminished, and variables in the flow tend to become "one-way" properties. Thus, when modelling certain situations with high Péclet numbers, simpler computational models can be adopted.[1]

A flow will often have different Péclet numbers for heat and mass. This can lead to the phenomenon of double diffusive convection.

In the context of particulate motion, the Péclet number has also been called Brenner number, with symbol Br, in honour of Howard Brenner.[2]

Other usages

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The Péclet number also finds applications beyond transport phenomena, as a general measure for the relative importance of the random fluctuations and of the systematic average behavior in mesoscopic systems.[3]

See also

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References

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  1. ^ Patankar, Suhas V. (1980). Numerical Heat Transfer and Fluid Flow. New York: McGraw-Hill. p. 102. ISBN 0-89116-522-3.
  2. ^ Promoted by S. G. Mason in publications from circa 1977 onward, and adopted by a number of others.[who?]
  3. ^ Gommes, Cedric; Tharakan, Joe (2020). "The Péclet number of a casino: Diffusion and convection in a gambling context". American Journal of Physics. 88 (6): 439. Bibcode:2020AmJPh..88..439G. doi:10.1119/10.0000957. S2CID 219432227.

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Jean Claude Eugène Péclet

Jean Claude Eugène Péclet (10 February 1793 – 6 December 1857) was a French physicist. He was born in Besançon, France. Péclet became, in 1812, one of

Magnetic Reynolds number

root-mean-square value. The magnetic Reynolds number has a similar form to both the Péclet number and the Reynolds number. All three can be regarded as giving

Reynolds number

Péclet number and the magnetic Reynolds number. These are therefore related to Re by-products with ratios of diffusivities, namely the Prandtl number

Marangoni number

tension. Thus as the Marangoni number compares flow and diffusion timescales it is a type of Péclet number. The Marangoni number is defined as: M a = advective

Rayleigh number

transport via convection at speed}}~u}}.} This means the Rayleigh number is a type of Péclet number. For a volume of fluid of size l {\displaystyle l} in all

Central differencing scheme

if the Peclet number is less than 2. Somewhat more dissipative Leads to oscillations in the solution or divergence if the local Peclet number is larger

Schmidt number

fluid (kg/m3) Pe is the Peclet Number Re is the Reynolds Number. The heat transfer analog of the Schmidt number is the Prandtl number (Pr). The ratio of thermal

Taylor dispersion

dispersion for large Peclet numbers. The analysis was later generalized by Rutherford Aris for arbitrary values of the Peclet number, and hence the process