A thin instrumented fin of length and large span is towed lengthwise through still…

PHYSICS · Multi-part · Fermi University Physics · Fluids & Continuum Physics · Viscous flow and dynamical similarity · Viscous flow and dynamical similarity

Fluid Dynamics, Ch The boundary layer: Prandtl's equations and the Blasius solution

Problem

A thin instrumented fin of length L=1.0 mL = 1.0\,\text{m} and large span is towed lengthwise through still water at constant speed U=0.20 m s−1U = 0.20\,\text{m s}^{-1}, so that in the fin's own frame a uniform stream of speed UU passes over each face with a laminar boundary layer and no pressure gradient imposed by the outer flow. Water properties are ρ=998 kg m−3\rho = 998\,\text{kg m}^{-3}, μ=1.00×10−3 Pa s\mu = 1.00\times10^{-3}\,\text{Pa s}. ((a)) State the condition on ∂p/∂y\partial p/\partial y that the boundary-layer scaling gives for this flow, and use it together with the definition of the momentum thickness δ2\delta_2 to write the momentum integral equation for zero pressure gradient in the form τw=ρU2 dδ2/dx\tau_w = \rho U^2\,d\delta_2/dx. ((b)) Using the Blasius result δ2(x)=0.664νx/U\delta_2(x) = 0.664\sqrt{\nu x/U}, integrate τw\tau_w from the leading edge to x=Lx = L to obtain the drag per unit width on one face of the fin, and show that the drag coefficient CD=D/(12ρU2L)C_D = D/(\tfrac12\rho U^2 L) obeys CD=1.328/ReLC_D = 1.328/\sqrt{Re_L}. ((c)) Compute ReLRe_L, check that the layer is laminar over the whole fin (transition is not observed below Rex≈3×105Re_x \approx 3\times10^{5}), and evaluate CDC_D and the drag per unit width on one face.

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