- Access by Xinjiang University
Revisiting the quest for a universal log-law and the role of pressure gradient in “canonical” wall-bounded turbulent flows
Phys. Rev. Fluids 2, 094602 – Published 13 September, 2017
DOI: https://doi.org/10.1103/PhysRevFluids.2.094602
Abstract
The trinity of so-called “canonical” wall-bounded turbulent flows, comprising the zero pressure gradient turbulent boundary layer, abbreviated ZPG TBL, turbulent pipe flow, and channel/duct flows has continued to receive intense attention as new and more reliable experimental data have become available. Nevertheless, the debate on whether the logarithmic part of the mean velocity profile, in particular the Kármán constant , is identical for these three canonical flows or flow-dependent is still ongoing. In this paper, the asymptotic matching requirement of equal in the logarithmic overlap layer, which links the inner and outer flow regions, and in the expression for the centerline/free-stream velocity is reiterated and shown to preclude a universal logarithmic overlap layer in the three canonical flows. However, the majority of pipe and channel flow studies at friction Reynolds numbers below extract from near-wall profiles the same of 0.38–0.39 as in the ZPG TBL. This apparent contradiction is resolved by a careful reanalysis of high-quality mean velocity profiles in the Princeton “Superpipe” and other pipes, channels, and ducts, which shows that the mean velocity in a near-wall region extending to around 700 “+” units in channels and ducts and 500 “+” units in pipes is the same as in the ZPG TBL. In other words, all the “canonical” flow profiles contain the lower end of the ZPG TBL log-region, which starts at a wall distance of “+” units with a universal of . This interior log-region is followed by a second logarithmic region with a flow specific , which increases monotonically with pressure gradient. This second, exterior log-layer is the actual overlap layer matching up to the outer expansion, which implies equality of the exterior and obtained from the evolution of the respective centerline velocity with Reynolds number. The location of the switch-over point implies furthermore that this second log-layer only becomes clearly identifiable, i.e., separated from the wake region, for well beyond (see Fig. 1). This explains the discrepancies between the Kármán constants of 0.38–0.39, extracted from near-wall pipe profiles below and the 's obtained from the evolution of the centerline velocity with Reynolds number. The same analysis is successfully applied to velocity profiles in channels and ducts even though experiments and numerical simulations have not yet reached Reynolds numbers where the different layers have even started to clearly separate.
Physics Subject Headings (PhySH)
Article Text
References (49)
- L. Prandtl, Bericht über Untersuchungen zur ausgebildeten Turbulenz, ZAMM 5, 136 (1925).
- Th. von Kármán, Turbulence and skin friction, J. Aero. Sci. 1, 1 (1934).
- A. Segalini, R. Örlü, and P. H. Alfredsson, Uncertainty analysis of the von Kármán constant, Exp. Fluids 54, 1460 (2013).
- F. H. Clauser, The turbulent boundary layer, Adv. Mech. 4, 1 (1956).
- T. Wei, R. Schmidt, and P. McMurtry, Comment on the Clauser chart method for determining the friction velocity, Exp. Fluids 38, 695 (2005).
- L. H. Tanner and L. G. Blows, A study of the motion of oil films on surfaces in air flow, with application to the measurement of skin friction, J. Phys. E: Sci. Intruments 9, 194 (1976).
- H. H. Fernholz, G. Janke, M. Schober, P. M. Wagner, and D. Warnack, New developments and applications of skin-friction measuring techniques, Meas. Sci. Technol. 7, 1396 (1996).
- M. V. Zagarola and A. J. Smits, Scaling of the Mean Velocity Profile for Turbulent Pipe Flow, Phys. Rev. Lett. 78, 239 (1997).
- H. M. Nagib and K. A. Chauhan, Variations of von Kármán coefficient in canonical flows, Phys. Fluids 20, 101518 (2008).
- R. Örlü, J. H. M. Fransson, and P. H. Alfredsson, On near wall measurements of wall bounded flows — The necessity of an accurate determination of the wall position, Progr. Aero. Sci. 46, 353 (2010).
- I. Marusic, J. P. Monty, M. Hultmark, and A. J. Smits, On the logarithmic region in wall turbulence, J. Fluid Mech. Rapids 716, R3 (2013).
- D. E. Coles, The law of the wake in the turbulent boundary layer, J. Fluid Mech. 1, 191 (1956).
- P. A. Monkewitz and H. M. Nagib, How comparable are the three “canonical” turbulent flows? in Proceedings of ICTAM 2016, Vol. 2, Montreal, Canada, edited by J. M. Floryan (IUTAM, 2017), pp. 484.
- M. V. Zagarola and A. J. Smits, Mean-flow scaling of turbulent pipe flow, J. Fluid Mech. 373, 33 (1998).
- B. J. McKeon, J. Li, W. Jiang, J. F. Morrison, and A. J. Smits, Further observations on the mean velocity distribution in fully developed pipe flow, J. Fluid Mech. 501, 135 (2004).
- S. C. C. Bailey, M. Hultmark, J. P. Monty, P. H. Alfredsson, M. S. Chong, R. D. Duncan, J. H. M. Fransson, N. Hutchins, I. Marusic, B. J. McKeon, H. M. Nagib, R. Örlü, A. Segalini, A. J. Smits, and R. Vinuesa, Obtaining accurate mean velocity measurements in high Reynolds number turbulent boundary layers using Pitot tubes, J. Fluid Mech. 715, 642 (2013).
- V. Kulandaivelu, Evolution and structure of zero pressure gradient turbulent boundary layer, Ph.D. thesis, University of Melbourne (2011).
- K. A. Chauhan, P. A. Monkewitz, and H. M. Nagib, Criteria for assessing experiments in zero pressure gradient boundary layers, Fluid Dynam. Res. 41, 021404 (2009).
- J. C. Rotta, Turbulent boundary layers in incompressible flow, Prog. Aero. Sci. 2, 1 (1962).
- P. A. Monkewitz, K. A. Chauhan, and H. M. Nagib, Self-consistent high-Reynolds-number asymptotics for zero-pressure-gradient turbulent boundary layers, Phys. Fluids 19, 115101 (2007).
- I. Marusic, B. J. McKeon, P. A. Monkewitz, H. M. Nagib, A. J. Smits, and K. R. Sreenivasan, Wall-bounded turbulent flows at high Reynolds numbers: Recent advances and key issues, Phys. Fluids 22, 065103 (2010).
- A. Segalini, J.-D. Rüedi, and P. A. Monkewitz, Systematic errors of skin-friction measurements by oil-film interferometry, J. Fluid Mech. 773, 298 (2015).
- J. Nikuradse, Gesetzmässigkeiten der turbulenten Strömung in glatten Rohren, VDI Forschungsheft (English translation: NASA TT F-10, 359) 365, 1 (1932).
- N. Furuichi, Y. Terao, Y. Wada, and Y. Tsuji, Friction factor and mean velocity profile for pipe flow at high Reynolds numbers, Phys. Fluids 27, 095108 (2015).
- A. Talamelli, F. Persiani, J. H. M. Fransson, P. H. Alfredsson, A. V. Johansson, H. M. Nagib, J.-D. Ruedi, K. R. Sreenivasan, and P. A. Monkewitz, CICLoPE—A response to the need for high Reynolds number experiments, Fluid Dynam. Res. 41, 021407 (2009).
- T. Fiorini, Turbulent Pipe Flow—High Resolution Measurements in CICLoPE, Ph.D. thesis, University of Bologna (2017).
- R. Örlü, T. Fiorini, A. Segalini, G. Bellani, A. Talamelli, P. H. Alfredsson, Reynolds stress scaling in pipe flow turbulence—First results from CICLoPE, Phil. Trans. R. Soc. A 375, 20160187 (2016).
- E. S. Zanoun, F. Durst, O. Bayoumy, and A. Al-Salaymeh, Wall skin friction and mean velocity profiles of fully developed turbulent pipe flows, Exp. Thermal Fluid Sci. 32, 249 (2007).
- B. J. McKeon and A. J. Smits, Static pressure correction in high Reynolds number fully developed turbulent pipe flow, Meas. Sci. Tech. 13, 1608 (2002).
- B. J. McKeon, J. D. Li, W. Jiang, J. F. Morrison, and A. J. Smits, Pitot probe corrections in fully-developed turbulent pipe flow, Meas. Sci. Tech. 14, 1449 (2003).
- R. Vinuesa, R. D. Duncan, and H. M. Nagib, Alternative interpretation of the superpipe data and motivation for ciclope: The effect of decreasing viscous length scale, Eur. J. Mech. B Fluids 58, 109 (2016).
- J. J. Allen, M. A. Shockling, and A. J. Smits, Evaluation of a universal transitional resistance diagram for pipes with honed surfaces, Phys. Fluids 17, 121702 (2005).
- S. C. C. Bailey, M. Vallikivi, M. Hultmark, and A. J. Smits, Estimating the value of von Kármán's constant in turbulent pipe flow, J. Fluid Mech. 749, 79 (2014).
- M. Hultmark, M. Vallikivi, S. C. C. Bailey, and A. J. Smits, Turbulent Pipe Flow at Extreme Reynolds Numbers, Phys. Rev. Lett. 108, 094501 (2012).
- A. E. Perry and C. J. Abell, Asymptotic similarity of turbulence structures in smooth- and rough-walled pipes, J. Fluid Mech. 79, 785 (1977).
- J. P. Monty, Developments in smooth wall turbulent duct flows, Ph.D. thesis, University of Melbourne (2005).
- J. Klewicki, J. Philip, I. Marusic, K. Chauhan, and C. Morrill-Winter, Self-similarity in the inertial region of wall turbulence, Phys. Rev. E 90, 063015 (2014).
- P. A. Monkewitz and H. M. Nagib, Large Reynolds number asymptotics of the stream-wise normal stress in ZPG turbulent boundary layers, J. Fluid Mech. 783, 474 (2015).
- R. Vinuesa and H. M. Nagib, Enhancing the accuracy of measurement techniques in high reynolds number turbulent boundary layers for more representative comparison to their canonical representations, Eur. J. Mech. B Fluids 55, Part 2, 300 (2016).
- R. Vinuesa, E. Bartrons, D. Chiu, K. M. Dressler, J.-D. Rüedi, Y. Suzuki, and H. M. Nagib, New insight into flow development and two dimensionality of turbulent channel flows, Exp. Fluids 55, 1759 (2014).
- R. Vinuesa, A. Noorani, A. Lozano-Durán, G. K. El Khoury, P. Schlatter, P. F. Fischer, and H. M. Nagib, Aspect ratio effects in turbulent duct flows studied through direct numerical simulation, J. Turbul. 15, 677 (2014).
- S. Hoyas and J. Jiménez, Scaling of the velocity fluctuations in turbulent channels up to , Phys. Fluids 18, 011702 (2006).
- A. Lozano-Durán and J. Jiménez, Effect of the computational domain on direct numerical simulations of turbulent channels up to , Phys. Fluids 26, 011702 (2014).
- M. Lee and R. D. Moser, Direct numerical simulation of turbulent channel flow up to , J. Fluid Mech. 774, 395 (2015).
- L. Thais, G. Mompean, and T. Gatski, Spectral analysis of turbulent viscoelastic and newtonian channel flows, J. Non-Newtonian Fluid Mech. 200, 165 (2013).
- E. S. Zanoun, F. Durst, and H. M. Nagib, Evaluating the law of the wall in two-dimensional fully developed turbulent channel flows, Phys. Fluids 15, 3079 (2003).
- M. P. Schultz and K. A. Flack, Reynolds number scaling of turbulent channel flow, Phys. Fluids 25, 025104 (2013).
- H. M. Nagib, P. A. Monkewitz, L. Moscotelli, T. Fiorini, G. Bellani, X. Zheng, and A. Talamelli, Centerline Kármán “constant” revisited and contrasted to log-layer Kármán constant at CICLoPE, in Proceedings of TSFP10, Chicago, IL, edited by H. M. Nagib and A. J. Smits (2017).
- Paolo Luchini, Universality of the Turbulent Velocity Profile, Phys. Rev. Lett. 118, 224501 (2017).