Entrainment across a sheared density interface in a cavity flow
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The entrainment of fluid across a sheared density interface has been examined experimentally in a purging cavity flow. In this flow, a long straight cavity with sloped entry and exit boundaries is located in the base of a straight open channel. Dense cavity fluid is entrained from ...
See moreThe entrainment of fluid across a sheared density interface has been examined experimentally in a purging cavity flow. In this flow, a long straight cavity with sloped entry and exit boundaries is located in the base of a straight open channel. Dense cavity fluid is entrained from the cavity into the turbulent overflow. The cavity geometry has been designed to ensure there is no separation of the overflow in the cavity region, with the goal of avoiding cavity-specific entrainment mechanisms as have been encountered in most previous experiments using similar arrangements. Results are obtained over a bulk Richardson number range Rib=gΔρD/ρ0U2b=1 to 19, where D and Ub are the depth of the mixed layer and bulk velocity in the cavity, respectively. The experiments cover the Reynolds number range Re=UbD/ν=7100 to 15 100 and interface length to mixed layer depth ratios of 2.4 to 16. Particle image velocimetry and laser induced fluorescence measurements indicate the flow regime over this entire range is one dominated by the Holmboe wave instability. The non-dimensional entrainment rate, E=ue/Ub , is shown to scale with the bulk Richardson number. We find that the entrainment scaling E=CRi−1.38b applies over the entire experimental range, with no apparent dependence on interface length. The exponent in the scaling is similar to previous non-cavity-based sheared interface flows, however, the constant C is up to an order of magnitude smaller. Close agreement is, however, obtained by instead correlating entrainment with the local gradient Richardson number centred on the interface, rather than bulk quantities. We obtain E=0.0021Ri−0.63g for data over 10<Rig<50 , where Rig=⟨g∂ρ/ρ0∂z⟩/⟨(∂U/∂z)2⟩ . The density interface is much thinner and therefore more stable in the present flow configuration compared with other published results for the same bulk Richardson number. We suggest that our configuration ensures a sharp mixing layer profile at the upstream end of the cavity even at relatively low bulk Richardson numbers of Rib=1 and that the reduced mixing in the Holmboe wave regime allows the interface to retain its sharp character over the cavity length, resulting in weak sensitivity to cavity length.
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See moreThe entrainment of fluid across a sheared density interface has been examined experimentally in a purging cavity flow. In this flow, a long straight cavity with sloped entry and exit boundaries is located in the base of a straight open channel. Dense cavity fluid is entrained from the cavity into the turbulent overflow. The cavity geometry has been designed to ensure there is no separation of the overflow in the cavity region, with the goal of avoiding cavity-specific entrainment mechanisms as have been encountered in most previous experiments using similar arrangements. Results are obtained over a bulk Richardson number range Rib=gΔρD/ρ0U2b=1 to 19, where D and Ub are the depth of the mixed layer and bulk velocity in the cavity, respectively. The experiments cover the Reynolds number range Re=UbD/ν=7100 to 15 100 and interface length to mixed layer depth ratios of 2.4 to 16. Particle image velocimetry and laser induced fluorescence measurements indicate the flow regime over this entire range is one dominated by the Holmboe wave instability. The non-dimensional entrainment rate, E=ue/Ub , is shown to scale with the bulk Richardson number. We find that the entrainment scaling E=CRi−1.38b applies over the entire experimental range, with no apparent dependence on interface length. The exponent in the scaling is similar to previous non-cavity-based sheared interface flows, however, the constant C is up to an order of magnitude smaller. Close agreement is, however, obtained by instead correlating entrainment with the local gradient Richardson number centred on the interface, rather than bulk quantities. We obtain E=0.0021Ri−0.63g for data over 10<Rig<50 , where Rig=⟨g∂ρ/ρ0∂z⟩/⟨(∂U/∂z)2⟩ . The density interface is much thinner and therefore more stable in the present flow configuration compared with other published results for the same bulk Richardson number. We suggest that our configuration ensures a sharp mixing layer profile at the upstream end of the cavity even at relatively low bulk Richardson numbers of Rib=1 and that the reduced mixing in the Holmboe wave regime allows the interface to retain its sharp character over the cavity length, resulting in weak sensitivity to cavity length.
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Date
2018Source title
Journal of Fluid MechanicsVolume
835Publisher
Cambridge University PressFunding information
ARC DP150100912Licence
Creative Commons Attribution-NonCommercial-NoDerivatives 4.0Faculty/School
Faculty of Engineering, School of Aerospace Mechanical and Mechatronic EngineeringShare