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2015 | OriginalPaper | Buchkapitel

17. Convective Material Transport

verfasst von : Roberto Mauri

Erschienen in: Transport Phenomena in Multiphase Flows

Verlag: Springer International Publishing

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Abstract

In this Chapter we study the material transport (in terms of mass or moles) of a dilute solute dissolved in a solvent. As we have seen in Sect. 14.​3, at leading order the average velocity of a mixture in the dilute limit equals the solvent velocity, so that the material transport reduces to a linear problem, as both diffusive and convective fluxes are linear functions of the concentration difference. Accordingly, the governing equations of mass transport in the dilute limit are identical as those of heat transport, so that most of the considerations that we made in Chap. 13 can be extended here. In particular, in Sects. 17.1 and 17.2 we study the mass boundary layer, with its dependence on the fluid velocity and the geometry of the problem. Then, in Sect. 17.3, we focus on the case where there is a mass boundary layer, with no momentum boundary layer, occurring when the material Peclet number is large and concomitantly the Reynolds number is small. The material boundary layer is further examined in Sect. 17.4, using the integral approximation described in Sect. 7.​7. Finally, in Sect. 17.5, we apply the quasi steady state approximation to solve important problems of mass transfer, related to particle growth or consumption.

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Fußnoten
1
Here, Pe denotes the material Peclet number, that is the ratio between convective and diffusive fluxes in the material (i.e., mass- or mole-based) transport of a chemical species. As we saw in Sects. 3.​2 and 13.​1, Pe may also indicate the thermal Peclet number; therefore, in this Chapter, the material Peclet number is sometimes denoted as Pe M .
 
2
The Leveque approximation describes the mass or heat exchange of a fluid in laminar flow in the entrance region of a tube, when the solute concentrations (or the temperatures) at the entrance and at the wall are specified (see Problem 17.1). The case of a fluid flowing past a submerged body is more complicated, because γ depends on x and, consequently, by continuity, the transversal velocity component is not null. Nevertheless, the results that are obtained in the general case are qualitatively similar to the ones that are obtained using the Leveque approximation.
 
3
As we discussed in Sect. 8.​2, this reasoning is based on the assumption that the problem admits a unique solution. Therefore, if at the end of this procedure we find a solution that satisfies all the assumptions that we have made on the way, we do not have to go on looking for another solution.
 
4
In the case of a flow past a sphere, we obtain: Sh = 1.249 Pe 1/3 , where Sh and Pe are defined in terms of the sphere radius R [see Leal (pp. 513–525)]. This confirms that the results obtained with the Leveque approximation can be applied also to more complex geometries.
 
Metadaten
Titel
Convective Material Transport
verfasst von
Roberto Mauri
Copyright-Jahr
2015
DOI
https://doi.org/10.1007/978-3-319-15793-1_17

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