The UMIST-N Near-Wall Treatment Applied to Periodic Channel Flow
The UMIST-N Near-Wall Treatment Applied to Periodic Channel Flow
The UMIST-N Near-Wall Treatment Applied to Periodic Channel Flow
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CHAPTER 5. RESULTS 73<br />
Integrating with respect <strong>to</strong> y,<br />
δ <br />
∂<br />
1 ∂ 〈P 〉<br />
〈U〉 dy = −<br />
y|<br />
∂t<br />
ρ ∂x<br />
y=δ<br />
<br />
τ <br />
y=0 + <br />
ρ<br />
0<br />
τ=0<br />
τ=τw<br />
Dividing by δ and noting that 1<br />
δ<br />
〈U〉 dy = U, Equation 5.7 becomes<br />
δ 0<br />
dU<br />
dt<br />
+ τw<br />
ρδ<br />
∂ 〈P 〉<br />
= −1<br />
ρ ∂x<br />
(5.7)<br />
(5.8)<br />
Thus, in unsteady channel flow, the driving pressure gradient applies energy<br />
<strong>to</strong> both overcome a wall shear stress and <strong>to</strong> accelerate the flow. <strong>The</strong> fact that<br />
peaks and troughs in U are underpredicted in Figure 5.5 indicates that dU<br />
dt is<br />
underestimated by the turbulence models. τw also displays a lower amplitude<br />
of variation than expected, as seen in Figure 5.6. This is consistent with<br />
<br />
<br />
(Equation 5.1). Together, these<br />
Figure 5.5, since τw is a function of ∂〈U〉<br />
∂y<br />
results suggest that the energy is added <strong>to</strong> and removed from the flow at a<br />
less than realistic rate.<br />
<strong>The</strong> equality in Equation 5.8 appears <strong>to</strong> be compromised when using these<br />
turbulence models in periodic flow. In terms of the x-momentum equation<br />
(Equation 3.5), this suggests that the models are not as well tuned <strong>to</strong> predict<br />
〈uv〉 in periodic channel flow as in steady channel flow. Errors in predicting<br />
〈uv〉 produce deviations in 〈U〉, particularly farther from the wall, as seen in<br />
Figures 5.11 & 5.12. This effects the dU<br />
dt<br />
y=0<br />
term in Equation 5.8.<br />
Figures 5.7, 5.8, 5.9 & 5.10 show flow variables plotted as a function of phase<br />
angle at various locations throughout the channel (y/δ = 0.1, 0.2, 0.5 & 0.9,<br />
respectively).<br />
Results for the k-ε log law do not appear in Figure 5.7, because y/δ = 0.1<br />
is outside the calculated flow field when the log law is used. In Figure 5.8,