 $Re_{D}$  from
 $Re_{D}$  from   $3.9\times 10^{3}$  to
 $3.9\times 10^{3}$  to   $8.5\times 10^{5}$ : a skin-friction perspective
 $8.5\times 10^{5}$ : a skin-friction perspectivePublished online by Cambridge University Press: 05 May 2017
We present wall-resolved large-eddy simulations (LES) of flow over a smooth-wall circular cylinder up to   $Re_{D}=8.5\times 10^{5}$ , where
 $Re_{D}=8.5\times 10^{5}$ , where   $Re_{D}$  is Reynolds number based on the cylinder diameter
 $Re_{D}$  is Reynolds number based on the cylinder diameter   $D$  and the free-stream speed
 $D$  and the free-stream speed   $U_{\infty }$ . The stretched-vortex subgrid-scale (SGS) model is used in the entire simulation domain. For the sub-critical regime, six cases are implemented with
 $U_{\infty }$ . The stretched-vortex subgrid-scale (SGS) model is used in the entire simulation domain. For the sub-critical regime, six cases are implemented with   $3.9\times 10^{3}\leqslant Re_{D}\leqslant 10^{5}$ . Results are compared with experimental data for both the wall-pressure-coefficient distribution on the cylinder surface, which dominates the drag coefficient, and the skin-friction coefficient, which clearly correlates with the separation behaviour. In the super-critical regime, LES for three values of
 $3.9\times 10^{3}\leqslant Re_{D}\leqslant 10^{5}$ . Results are compared with experimental data for both the wall-pressure-coefficient distribution on the cylinder surface, which dominates the drag coefficient, and the skin-friction coefficient, which clearly correlates with the separation behaviour. In the super-critical regime, LES for three values of   $Re_{D}$  are carried out at different resolutions. The drag-crisis phenomenon is well captured. For lower resolution, numerical discretization fluctuations are sufficient to stimulate transition, while for higher resolution, an applied boundary-layer perturbation is found to be necessary to stimulate transition. Large-eddy simulation results at
 $Re_{D}$  are carried out at different resolutions. The drag-crisis phenomenon is well captured. For lower resolution, numerical discretization fluctuations are sufficient to stimulate transition, while for higher resolution, an applied boundary-layer perturbation is found to be necessary to stimulate transition. Large-eddy simulation results at   $Re_{D}=8.5\times 10^{5}$ , with a mesh of
 $Re_{D}=8.5\times 10^{5}$ , with a mesh of   $8192\times 1024\times 256$ , agree well with the classic experimental measurements of Achenbach (J. Fluid Mech., vol. 34, 1968, pp. 625–639) especially for the skin-friction coefficient, where a spike is produced by the laminar–turbulent transition on the top of a prior separation bubble. We document the properties of the attached-flow boundary layer on the cylinder surface as these vary with
 $8192\times 1024\times 256$ , agree well with the classic experimental measurements of Achenbach (J. Fluid Mech., vol. 34, 1968, pp. 625–639) especially for the skin-friction coefficient, where a spike is produced by the laminar–turbulent transition on the top of a prior separation bubble. We document the properties of the attached-flow boundary layer on the cylinder surface as these vary with   $Re_{D}$ . Within the separated portion of the flow, mean-flow separation–reattachment bubbles are observed at some values of
 $Re_{D}$ . Within the separated portion of the flow, mean-flow separation–reattachment bubbles are observed at some values of   $Re_{D}$ , with separation characteristics that are consistent with experimental observations. Time sequences of instantaneous surface portraits of vector skin-friction trajectory fields indicate that the unsteady counterpart of a mean-flow separation–reattachment bubble corresponds to the formation of local flow-reattachment cells, visible as coherent bundles of diverging surface streamlines.
 $Re_{D}$ , with separation characteristics that are consistent with experimental observations. Time sequences of instantaneous surface portraits of vector skin-friction trajectory fields indicate that the unsteady counterpart of a mean-flow separation–reattachment bubble corresponds to the formation of local flow-reattachment cells, visible as coherent bundles of diverging surface streamlines.