1994
DOI: 10.1016/0017-9310(94)90186-4
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Transient deformation and evaporation of droplets at intermediate Reynolds numbers

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Cited by 43 publications
(9 citation statements)
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“…(see e.g. [64,66,[358][359][360][361][362][363][364][365]), their analytical solutions (see e.g. [366]) and asymptotic analyses in the limiting cases (see e.g.…”
Section: Coupled Solutionsmentioning
confidence: 99%
“…(see e.g. [64,66,[358][359][360][361][362][363][364][365]), their analytical solutions (see e.g. [366]) and asymptotic analyses in the limiting cases (see e.g.…”
Section: Coupled Solutionsmentioning
confidence: 99%
“…Regarding the coupled problem of droplet breakup and evaporation, this has not yet been studied in detail except in the CFD works of [55][56][57][58][59][60]. Haywood et al [55,56] showed that for droplets under steady or unsteady (oscillatory) deformation, the quasi-steady correlations for Nusselt (Nu) and Sherwood (Sh) numbers are still valid when a volume-equivalent diameter is used, Mao et al [57] showed that the mass transfer from deformed droplets is mainly controlled by the Peclet (Pe) number, while the We number has a small impact only at high Pe numbers. Hase and Weigand [58] studied the effect of droplet deformation on the heat transfer enhancement and they found that this increases due to the oscillatory droplet motion and the increased surface area of the deformed droplets; moreover, the steady-state classical correlations for the Nu number, under-predict the heat transfer at the beginning of the simulation.…”
Section: Introductionmentioning
confidence: 99%
“…The first was used by Renksizbulut and Yuen [ 1] with the moving mesh method to simulate droplet evaporation, where variable properties on evaporation were also investigated [2], Haywood etal. [3] used a similar model where deformed droplets are considered.…”
Section: Introductionmentioning
confidence: 99%