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<https://discovery.ucl.ac.uk/id/eprint/10187018> <http://purl.org/dc/terms/title> "Forced convection past a circular cylinder in a planar Poiseuille flow"^^<http://www.w3.org/2001/XMLSchema#string> .
<https://discovery.ucl.ac.uk/id/eprint/10187018> <http://purl.org/ontology/bibo/abstract> "In this work the transfer of a passive scalar (temperature) from a circular cylinder (radius R) in a planar Poiseuille flow (height\r\n2h) is investigated with numerical simulations. The study varies the channel half-height to cylinder radius ϵ = h/R, the inertial\r\nparameter Λ = (UcR/ν)(h/R)\r\n2\r\nand the Peclet number ´ Pe = UcR/α, where Uc is the midplane velocity, ν is the kinematic viscosity\r\nand α is the thermal diffusivity. There has been significant amount of work for ϵ ≫ 1, therefore this work will focus on the range,\r\n0.03 ≤ ϵ ≤ 1, which has been chosen to show the effect of geometry and inertia on the flow features and the subsequent transfer.\r\nAs ϵ is decreased the Nusselt number increases and this behaviour is explained with velocity and temperature profiles.\r\nParticularly for ϵ = 0.03, the local Nusselt number has a significant vertical variation (in the z-direction) when Λ and Pe are\r\nincreased past certain values. For Λ ≪ 1 and Pe > 103\r\nthis is due to the non-uniform incident flow present in the Hele-Shaw\r\ncell while for Λ = O(1), it is the secondary flow that is induced at the sides of the cylinder. For these latter flows the transfer in\r\nthe midplane is reduced relative to near the side walls, due to the triple turning point radial velocity profile adjacent to the circular\r\ncylinder. For Λ ≤ 1, the Nusselt number is only a function of Pe. However, for Λ > 1, the secondary flow results in a slightly\r\nincreased Nusselt number."^^<http://www.w3.org/2001/XMLSchema#string> .
<https://discovery.ucl.ac.uk/id/eprint/10187018> <http://purl.org/dc/terms/date> "2024-02" .
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