Please use this identifier to cite or link to this item: http://buratest.brunel.ac.uk/handle/2438/12469
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dc.contributor.authorHerlina, H-
dc.contributor.authorWissink, JG-
dc.date.accessioned2016-04-12T15:00:19Z-
dc.date.available2016-04-12T15:00:19Z-
dc.date.issued2016-
dc.identifier.citationJournal of Fluid Mechanics, 797: pp. 665 -682, (2016)en_US
dc.identifier.issn1469-7645-
dc.identifier.urihttp://bura.brunel.ac.uk/handle/2438/12469-
dc.description.abstractDirect numerical simulations were performed to investigate the effect of severe contamination on interfacial gas transfer in the presence of isotropic turbulence diffusing from below. A no-slip boundary condition was employed at the interface to model the severe contamination effect. The influence of both Schmidt number (Sc) and turbulent Reynolds number (RT ) on the transfer velocity (KL) was studied. In the range from Sc = 2 up to Sc = 500, it was found that KL ∝ Sc²/³, which is in agreement with predictions based on solid-liquid transport models, see e.g. Davies (Turbulence Phenomena 1972). For similar RT , the transfer velocity was observed to reduce significantly compared to the free-slip conditions. The reduction becomes more pronounced with increasing Schmidt number. Similar to the observation for free-slip conditions made by Theofanous et al. (Int. J. Heat Mass Transfer, 1976), the normalised KL in the present no-slip case was also found to depend on RT ‾¹/² and RT ‾¹/⁴ for small and large turbulent Reynolds numbers, respectively.en_US
dc.language.isoenen_US
dc.publisherCambridge University Press (CUP): STM Journalsen_US
dc.titleIsotropic-turbulence-induced mass transfer across a severely contaminated water surfaceen_US
dc.typeArticleen_US
dc.identifier.doihttp://dx.doi.org/10.1017/jfm.2016.278-
dc.relation.isPartOfJournal of Fluid Mechanics-
pubs.publication-statusAccepted-
Appears in Collections:Dept of Mechanical Aerospace and Civil Engineering Research Papers

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