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Favourable breakdown of the Reynolds analogy in turbulent heat transfer over streamwise-aligned longitudinal rib arrays

Published online by Cambridge University Press:  11 June 2026

Yusuke Kuwata*
Affiliation:
Mechanical Engineering, Osaka Metropolitan University , Osaka, Japan
*
Corresponding author: Yusuke Kuwata, ykuwata1919@gmail.com

Abstract

We performed a direct numerical simulation study on the breakdown of the Reynolds analogy over streamwise-aligned longitudinal rib arrays caused by Kelvin–Helmholtz (K–H) instability-induced turbulence. The purpose of this study was to elucidate the underlying physics responsible for the favourable breakdown of the Reynolds analogy, and gain better insight into the scaling of the dissimilar heat transfer enhancement and characteristics of the K–H instability-induced turbulence structure. Temperature was treated as a passive scalar with a Prandtl number of unity. The thermal and flow boundary conditions were prescribed such that the non-dimensional streamwise momentum and energy equations were similar. The results showed that the Reynolds analogy factor attains its maximum value when the spanwise-oriented turbulent structure associated with the K–H instability becomes energetic. The slip-to-bulk velocity ratio serves as an effective scaling parameter not only for the Reynolds analogy factor but also for quantifying the significance of turbulence structures induced by the K–H instability, and a moderate slip-to-bulk velocity ratio yields the largest Reynolds analogy factor. A conditional averaging analysis reveals that the K–H instability generates a counter-rotating vortex pair accompanied by streamwise-alternating turbulent fluctuations. The associated streamwise-alternating perturbations in pressure, velocity and temperature exhibit phase differences between them. The phase difference strengthens the negative correlation between the vertical velocity and temperature fluctuations, while reducing that between the vertical and streamwise velocity fluctuations within the rib arrays. As a result, the vertical turbulent heat flux is more significantly enhanced than the Reynolds shear stress within the rib arrays. Another consequence of the phase differences is the dissimilar modifications of the pressure correlation terms in the transport equations for turbulent heat and momentum fluxes. A budget analysis indicates that modifying the pressure correlation terms also serves to enhance the vertical heat flux more than the Reynolds shear stress, thereby reinforcing the favourably dissimilar heat transfer enhancement.

Information

Type
JFM Papers
Copyright
© The Author(s), 2026. Published by Cambridge University Press
Figure 0

Figure 1. Computational geometry of the longitudinal rib-roughened open-channel flows. Here, $H$ is the clear channel height, $h$ is the rib height, $s$ is the separation between the ribs and $w$ is the thickness of the rib. The streamwise and spanwise domain lengths are $L_x$ and $L_z$, respectively.

Figure 1

Table 1. Parameters of the DNS and rib arrays: friction Reynolds number $\textit{Re}_\tau =u_\tau H/\nu$, spanwise separation between the ribs $s$, thickness of a rib $w$, permeability of finite parallel rib arrays $K_\infty$, permeability Reynolds number $\textit{Re}_K=\sqrt {K_\infty }/\ell _v$ and square root of the groove cross-section $\ell _g = \sqrt {sh}$. The information for case 300 was obtained from Kuwata (2022a).

Figure 2

Table 2. Parameters related to the numerical set-up. Here, $\varDelta ^+=\varDelta /\ell _v$ is the inner-scaled grid spacing for the fine grid block, $L_x$ is the streamwise domain length and $L_z$ is the spanwise domain length.

Figure 3

Figure 2. Inner-scaled mean velocity $U^+={\langle \overline {u}\rangle }^+$ and temperature $\varTheta ^+={\langle \overline {\theta }\rangle }^+$ profiles: (a,b,c) $\textit{Re}_\tau =180$ and (d,e, f) $\textit{Re}_\tau =500$. The rib spacing, i.e. volume fraction $\varphi$ within the rib region, increases from left to right. The rib crest and base wall positions are $y/H=0$ and $y/H=-2/3$, respectively. The solid and dashed lines indicate the temperature $\varTheta ^+$ and velocity $U^+$, respectively.

Figure 4

Figure 3. Inner-scaled mean velocity $U^+$ profiles with (a,b) log–linear format and (c,d) defect form: (a,c) $\textit{Re}_\tau =180$ and (b,d) $\textit{Re}_\tau =500$. The smooth-wall results from Kim, Moin & Moser (1987) at $\textit{Re}_\tau =180$ and from Lluesma-Rodríguez et al. (2018) at $\textit{Re}_\tau =500$ are included for comparison.

Figure 5

Figure 4. (a,c) Velocity roughness functions $\Delta U^+$ and (b,d) temperature roughness function $\Delta \varTheta ^+$: (a,b) against the permeability Reynolds number $\textit{Re}_K=\sqrt {K_\infty }^+$ and (c,d) against the Darcy number $\sqrt {Da}=\sqrt {K_\infty }/H$. The thin lines in the figure are the approximate lines that indicate the trend of $\Delta U^+$ or $\Delta \varTheta ^+$. The results at $\textit{Re}_\tau =300$ were obtained from Kuwata (2022a).

Figure 6

Figure 5. Augmentation of the Stanton number $S_t/S_{t0}$ against that of the skin friction coefficient $C_{\!f}/C_{\!f0}$ from smooth-wall turbulence at the same $\textit{Re}_\tau$. The thin line is $S_t/S_{t0}=C_{\!f}/C_{\!f0}$, which means that the Reynolds analogy factor $\textit{RA}$ is the same as that for the smooth-wall turbulence $\textit{RA}_0$. The dashed line is the approximate line for the current results, $S_t/S_{t0} = (C_{\!f}/C_{\!f0})^{1.28}$. The results at $\textit{Re}_\tau =300$ are from Kuwata (2022a).

Figure 7

Figure 6. Modification of the Reynolds analogy factor $\textit{RA}=2S_t/C_{\!f}$ from the smooth-wall value $\textit{RA}_0=2S_{t0}/C_{\!f0}$. The results are plotted against the inner-scaled permeability $\textit{Re}_K$ in (a), against the outer-scaled permeability $\sqrt {Da}$ in (b) and against the slip-to-bulk velocity ratio $U_s/U_b$ in (c). The results at $\textit{Re}_\tau =300$ are from Kuwata (2022a).

Figure 8

Figure 7. Skin friction coefficient $C_{\!fy}$ and doubled Stanton number $2S_{ty}$ evaluated at position $y$ for $\textit{Re}_\tau =500$: (a) case 500-50, (b) case 500-80 and (c) case 500-96. The values at the rib crest ($y=0$) and base wall ($y/H=-2/3$) are denoted by squares.

Figure 9

Figure 8. The JPDF of spatiotemporally fluctuating skin friction coefficient $C^\prime_{\!f}$ and Stanton number $S^\prime_{t}$ on the rib crest at $y=0$ and vertical rib walls ($-2/3\lt y/H\lt 0$) for case 500-80. The lines for spatiotemporal Reynolds analogy $\textit{RA}^\prime = 2S^\prime_{t}/C^\prime_{\!f} = 1$, favourable breakdown $\textit{RA}^\prime = 1.4$ and unfavourable breakdown $\textit{RA}^\prime = 0.4$ are included. The vertical and horizontal lines indicate $\textit{RA}^\prime = \infty$ ($C^\prime_{\!f}=0$) and $\textit{RA}^\prime = 0$ ($S^\prime_{t}=0$), respectively.

Figure 10

Figure 9. Snapshots of streamwise velocity fluctuations above the rib crest at $y^+\simeq 10$: (a) case 180-50, (b) case 500-50, (c) case 180-60, (d) case 500-60, (e) case 180-80, (f) case 500-80, (g) case 180-90, (h) case 500-90, (i) case 180-96 and (j) case 500-96. Panels (a,c,e,g,i) and (b,d, f,h, j) show the results at $\textit{Re}_\tau =180$ and $\textit{Re}_\tau =500$, respectively. The porosity $\varphi$ increases from (a) to (j), and the position of the ribs is also shown.

Figure 11

Figure 10. Characteristic wavelength of the K–H instability scaled in viscous units, $\lambda _{\textit{KH}}^+$, in (a) and (b), and in outer units, $\lambda _{\textit{KH}}/H$, in (c): (a) $\lambda _{\textit{KH}}^+$ plotted against $\textit{Re}_K$, (b) $\lambda _{\textit{KH}}^+$ plotted against $\ell _s^+$ and (c) $\lambda _{\textit{KH}}/H$ plotted against $\sqrt {Da}$. The results for the densest case (180-050) and sparsest cases with $\varphi =0.96$ are excluded because no K–H-instability-induced turbulence was detected in these cases. The data at $\textit{Re}_\tau = 300$ were obtained from the snapshot database of Kuwata (2022a).

Figure 12

Figure 11. Intensity of the K–H instability-induced turbulence scaled in viscous units, $I_{\textit{KH}}^+$, in panels (a) and (b), and in outer units, $I_{\textit{KH}}/U_b^2$, in (c): (a) $I_{\textit{KH}}^+$ plotted against $\textit{Re}_K$, (b) $I_{\textit{KH}}^+$ plotted against $\ell _s^+$ and (c) $I_{\textit{KH}}/U_b^2$ plotted against $\sqrt {Da}$. The results for the densest case (180-050) and sparsest cases with $\varphi = 0.96$ are excluded because no K–H-instability-induced turbulence was detected in these cases. The data at $\textit{Re}_\tau = 300$ were obtained from the snapshot database of Kuwata (2022a).

Figure 13

Figure 12. Here we plot $\textit{RA}/\textit{RA}_0$ against the intensity of the K–H instability-induced turbulence, $I_{\textit{KH}}/U_b^2$. Intensity $I_{\textit{KH}}/U_b^2$ is assumed to be zero for the densest case (180-050) and sparsest cases with $\varphi =0.96$, where the K–H instability-induced turbulence is not detected. The results at $\textit{Re}_\tau =300$ were obtained from Kuwata (2022a).

Figure 14

Figure 13. (a) Turbulence intensities of streamwise $u^+_{\textit{rms}}$, vertical $v^+_{\textit{rms}}$ and spanwise $w^+_{\textit{rms}}$ components and (b) $u^+_{\textit{rms}}$ and temperature variance $\theta ^+_{\textit{rms}}$. The rib crest and base wall positions are $y/H=0$ and $y/H=-2/3$, respectively. The results for the significant favourable breakdown case of 500-0.8 are shown.

Figure 15

Figure 14. (a) Turbulent momentum and heat fluxes (Reynolds shear stress $R^+_{12}$ and vertical turbulent heat flux $H^+_{2}$) and (b) dispersion momentum and heat fluxes (dispersion shear stress $\mathcal{T}^+_{12}$ and vertical dispersion heat flux ${\mathcal{H}}_{2}$). The rib crest and base wall positions are $y/H=0$ and $y/H=-2/3$, respectively. The results for case 500-0.8 are shown.

Figure 16

Figure 15. Correlation coefficients for temperature–streamwise velocity $r_{1\theta }$, temperature–vertical velocity $r_{2\theta }$, and streamwise and vertical velocities $r_{12}$ for case 500-80.

Figure 17

Figure 16. Turbulent Prandtl number $\textit{Pr}_t=\nu _t/\alpha _t$ in (3.6) and effective Prandtl number $\textit{Pr}_{\textit{eff}}$ in (3.7) for case 500-80. Note that computations of $\textit{Pr}_t$ and $\textit{Pr}_{\textit{eff}}$ are restricted to the region where the turbulent fluxes have a meaningful value $-R_{12}^+\gt 0.01$ and $-H_{2}^+\gt 0.01$.

Figure 18

Figure 17. The JPDF within the rib array region at $y/H=-0.1$ for case 500-80: (a) JPDF for $u^\prime-v^\prime$ space $P_{uv}$, (b) JPDF for $\theta ^\prime-v^\prime$ space $P_{v\theta }$, (c) contour lines of $P_{uv}$ and $P_{v\theta }$ with an interval of 0.02, (d) weighted JPDF for $u^\prime-v^\prime$ space $Pw_{uv}$, (e) weighted JPDF for $\theta ^\prime-v^\prime$ space $Pw_{v\theta }$ and (f) contour lines of $Pw_{uv}$ and $Pw_{v\theta }$ with an interval of 0.06.

Figure 19

Figure 18. Conditionally averaged fields around the downward flow events within the rib array at $y/H=-0.1$ in the $x{-}z$ plane along with the cross-sectional conditional average fluctuating velocity vectors for case 500-80: (a) streamwise velocity $[u^\prime]$, (b) temperature $[\theta ^\prime]$, (c) vertical velocity $[v^\prime]$ and (d) pressure $[p^\prime]$. The reference point is located at a centre $x-y$ plane between the neighbouring ribs and at $x^\prime = x-L_x/2=0$.

Figure 20

Figure 19. Conditionally averaged perturbations of the streamwise velocity, vertical velocity, pressure and temperature along the streamwise direction for case 500-80: (a) above the rib array at $y/H=0.2$ and (b) within the rib array at $y/H=-0.2$.

Figure 21

Figure 20. Comparison of the budget terms for $R_{12}^+$ and $H_2^+$ at $\textit{Re}_\tau =500$: (a) smooth-wall case, (b) rib array case 500-80 and (c) close-up view within the rib array for case 500-80. For comparison, the reference DNS results for the smooth-wall case at $\textit{Pr}=1$ and $\textit{Re}_\tau =500$ from Alcántara-Ávila & Hoyas (2021) are included as the open symbols in (a).

Figure 22

Figure 21. Comparison of the pressure–correlation terms in the transport equations of $R_{12}^+$ and $H_2^+$: (a) pressure–strain term $\varPhi ^{+}_{12}$, pressure diffusion term $D^{p+}_{12}$ and total contribution $\varPi _{12}^+=\varPhi ^+_{12}+D^{p+}_{12}$ and (b) pressure scrambling term $\varPhi ^{\theta +}_{2}$, pressure diffusion term $D^{p \theta +}_2$ and $\varPi ^{\theta +}_2=\varPhi ^{\theta +}_{2} + D^{p \theta +}_2$.

Figure 23

Figure 22. Comparison of the pressure–velocity ${\langle \overline {p^\prime u_i^\prime}\rangle }^+$ and pressure–temperature ${\langle \overline {p^\prime\theta ^\prime}\rangle }^+$ correlation terms for case 500-80.

Figure 24

Table 3. Parameters related to the numerical set-up. Here, $\varDelta ^+$ is the grid spacing in the wall unit, $L_x$ is the streamwise domain length and $L_z$ is the spanwise domain length. The grid is refined by 20 % for the fine case (180-80). The domain lengths are extended by 50 % in the $x$- and $z$-directions for the large case (180-80). For the higher $\textit{Re}_\tau$ cases at $\textit{Re}_\tau =500$, the grid dependency is tested by a simulation with a 30 % coarse grid for the coarse case (500-80). The streamwise and spanwise domain lengths are extended by 45 % from the baseline case for the coarse and large case (500-80).

Figure 25

Figure 23. Grid and domain sensitivity test results: (a) mean velocity for case 180-80, (b) turbulence intensities for case 180-80, (c) mean velocity for case 500-80 and (d) turbulence intensities for case 500-80. See table 3 for the parameters of the simulations.

Figure 26

Figure 24. Two-dimensional premultiplied spectra for vertical velocity fluctuations $(E_{vv}\kappa _x \kappa _z)^+$ for case 500-80 at $y^+ \simeq 10$ where $\kappa _x$ and $\kappa _z$ denote the streamwise and spanwise wavenumbers, respectively. The colour contour map with solid isolines denotes the results for case coarse and large (500-80) with the larger domain case ($L_x/H=8.7$ and $L_z/H=7.2$) and dashed isolines are for case coarse (500-80) with the baseline domain ($L_x/H=6$ and $L_z/H=5$). The vertical (horizontal) axis is the inner- or outer-scaled spanwise wavelength $\lambda _z^+$ ($\lambda _x^+$) or $\lambda _z/H$ ($\lambda _x/H$), respectively. See table 3 for the parameters of the simulations.

Figure 27

Figure 25. Diagnostic function based on $y$: (a) $\textit{Re}_\tau =180$ and (b) $\textit{Re}_\tau =500$.

Figure 28

Figure 26. (a) Diagnostic function based on $y+d_J$, (b) diagnostic function based on $y+d_S$ and (c) zero-plane displacements $d_J/H$ and $d_S/H$. The zero-plane displacement $d_J$ was obtained using the extended Jackson model for a pressure-driven flow (Breugem et al.2006), whereas $d_S$ was determined to ensure a better collapse of the diagnostic function onto the smooth-wall case within $300\lt y^+\lt 400$. Vertical lines indicate the intermediate line in the clear flow region at $y^+=\textit{Re}_\tau /2$. The results at $\textit{Re}_\tau =500$ are shown.

Figure 29

Figure 27. Velocity difference with respect to the smooth-wall profile, $U^+_{d}=U^+_{\textit{smooth}}-U^+_{\textit{rib}}$, where $U^+_{\textit{smooth}}$ and $U^+_{\textit{rib}}$ are the values for the smooth-wall and rib array cases at the same $\textit{Re}_\tau$: (a) $\textit{Re}_\tau =180$ and (b) $\textit{Re}_\tau =500$. The lower and upper limits of $U^+_{d}$ estimated in the range $\textit{Re}_\tau /2\lt y^+\lt \textit{Re}_\tau$ are denoted by dashed lines. Vertical lines indicate the intermediate line in the clear flow region at $y^+=\textit{Re}_\tau /2$.

Figure 30

Figure 28. The $x{-}z$ plane-averaged Reynolds analogy factor $\textit{RA}(y)=2S_{t}(y)/C_{\!f}(y)$: (a) $\textit{Re}_\tau =180$ and (b) $\textit{Re}_\tau =500$.