NivaarExam PrepOfficial exam papers ↗

22-Mec-B6 Advanced Fluid Mechanics · December 2016

Question 6 of 6: Boundary layer in an accelerating suction wind tunnel

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

Paper format. National Exams, December 2016 — 07-Mec-B6 Advanced Fluid Mechanics. Three hours, OPEN BOOK, any approved Sharp or Casio calculator permitted. Six questions are printed; page 1 states that any five of them constitute a complete paper for 100 marks, each question carries an equal 20 marks, and the item weights are shown in the left margin. No aid sheet is bound into the paper — the open-book rule is the candidate’s table source, so every compressible-flow ratio below is quoted in closed form rather than read off a chart. All six questions are solved here.

Reference texts. The solutions follow the conventions of the texts the EGBC syllabus recommends for this subject:

Question 6: Boundary layer in an accelerating suction wind tunnel (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantityFormNote
External velocityU0 = A x1/3accelerating, so dU0/dx > 0
Assumed profileu/U0 = 2(y/δ) − (y/δ)2parabolic, satisfies u = U0 and ∂u/∂y = 0 at y = δ
Displacement thicknessδ*/δ = 1/3from ∫(1 − u/U0)dy
Momentum thicknessθ/δ = 2/15from ∫(u/U0)(1 − u/U0)dy
Assumed growth lawδ = B xnwith δ = 0 at x = 0
Regimetwo-dimensional, laminar, constant propertiesν = μ/ρ

Find. The exponent n that makes the assumed growth law satisfy the momentum-integral equation, the resulting δ/x and local skin-friction coefficient in terms of Rex, and the average skin-friction coefficient over 0 ≤ x ≤ L referred to the exit velocity.

delta = B x1/3 u(y) U0 = A x1/3 accelerates downstream y x x = L
Figure 6 — The tunnel. The curved upper wall accelerates the core flow as U0 = A x1/3, and the boundary layer on the straight bottom wall grows like x1/3 as well, so δ/x actually shrinks downstream.

Approach. Substitute the two power laws and the profile constants into the Kármán momentum-integral equation, then match the powers of x to get n and match the coefficients to get B; everything else follows algebraically.

  1. Write the momentum-integral equation for a flow with a pressure gradient. For a two-dimensional incompressible boundary layer beneath an external velocity U0(x), $$\frac{\mathrm{d}\theta}{\mathrm{d}x} +\left(2\theta+\delta^{*}\right)\frac{1}{U_0}\frac{\mathrm{d}U_0}{\mathrm{d}x} =\frac{\tau_w}{\rho U_0^{2}} .$$ The bracket is what carries the effect of the acceleration; it disappears only for a flat plate in a uniform stream.
  2. Evaluate the wall shear from the assumed profile. Differentiating $u/U_0=2(y/\delta)-(y/\delta)^{2}$ at the wall, $$\tau_w=\mu\left.\frac{\partial u}{\partial y}\right|_{y=0}=\frac{2\mu U_0}{\delta} \quad\Longrightarrow\quad \frac{\tau_w}{\rho U_0^{2}}=\frac{2\nu}{U_0\delta}.$$
  3. Part (a) — substitute the two power laws. With $\theta=\tfrac{2}{15}\delta$, $\delta^{*}=\tfrac{1}{3}\delta$, $\delta=Bx^{n}$ and $U_0=Ax^{m}$ with m = 1/3, the left-hand side becomes $$\frac{2}{15}Bn\,x^{n-1}+\left(\frac{4}{15}+\frac{1}{3}\right)Bx^{n}\frac{m}{x} =Bx^{n-1}\left[\frac{2}{15}n+\frac{3}{5}m\right],$$ while the right-hand side is $$\frac{2\nu}{U_0\delta}=\frac{2\nu}{AB}x^{-m-n}.$$
  4. Match the exponents of x. The two sides can agree at every station only if $$n-1=-m-n \quad\Longrightarrow\quad n=\frac{1-m}{2}=\frac{1-\tfrac{1}{3}}{2},$$ $$\boxed{n=\tfrac{1}{3}}$$ so the layer grows as x1/3. This is slower than the x1/2 of a flat plate, which is exactly what a favourable pressure gradient should do: the accelerating core keeps thinning the layer relative to its own distance from the leading edge.
  5. Match the coefficients to obtain B. Substituting n = m = 1/3 into the bracket, $$\frac{2}{15}\left(\frac{1}{3}\right)+\frac{3}{5}\left(\frac{1}{3}\right) =\frac{2}{45}+\frac{9}{45}=\frac{11}{45},$$ so $B^{2}\dfrac{11}{45}=\dfrac{2\nu}{A}$ and $$\boxed{B=\sqrt{\frac{90\,\nu}{11\,A}}}$$
  6. Part (b) — convert to a Reynolds-number form. Since $\mathrm{Re}_x=U_0x/\nu=Ax^{4/3}/\nu$, we have $x^{-2/3}=\sqrt{A/(\nu\,\mathrm{Re}_x)}$, and therefore $$\frac{\delta}{x}=Bx^{n-1}=Bx^{-2/3}=\sqrt{\frac{90\nu}{11A}}\sqrt{\frac{A}{\nu\,\mathrm{Re}_x}},$$ $$\boxed{\frac{\delta}{x}=\sqrt{\frac{90}{11\,\mathrm{Re}_x}}=\frac{2.860}{\sqrt{\mathrm{Re}_x}}}$$ Both A and ν have cancelled, so the result is universal for this profile and this acceleration. For comparison the same parabolic profile on a flat plate gives 5.48/√Rex, so the favourable gradient here thins the layer by very nearly a factor of two.
  7. Part (c) — form the local skin-friction coefficient. From step 2, $$C_{fx}=\frac{\tau_w}{\tfrac{1}{2}\rho U_0^{2}}=\frac{4\nu}{U_0\delta} =\frac{4}{\mathrm{Re}_x}\left(\frac{x}{\delta}\right) =\frac{4}{\mathrm{Re}_x}\cdot\frac{\sqrt{\mathrm{Re}_x}}{2.860},$$ $$\boxed{C_{fx}=4\sqrt{\frac{11}{90}}\,\mathrm{Re}_x^{-1/2}=\frac{1.398}{\sqrt{\mathrm{Re}_x}}}$$ The coefficient of δ/x and the coefficient of Cfx are locked to one another through the profile constant, since Cfx = 4 ÷ (coefficient of δ/x).
  8. Part (d) — discover that the wall shear is constant along the tunnel. Writing the dimensional shear out, $$\tau_w=C_{fx}\frac{\rho U_0^{2}}{2} =1.398\left(\frac{\nu}{Ax^{4/3}}\right)^{1/2}\frac{\rho A^{2}x^{2/3}}{2} =\frac{1.398}{2}\rho A^{3/2}\nu^{1/2}\,x^{0},$$ so τw is independent of x. In general $\tau_w\propto x^{(3m-1)/2}$, and m = 1/3 is precisely the exponent that makes it uniform. That is the whole reason a suction tunnel is contoured this way: a test section with constant wall shear has a boundary layer whose growth is predictable and whose wall heat-transfer and skin-friction instrumentation reads the same at every station.
  9. Complete the averaging. Because the integrand is constant, $$\bar\tau_w=\frac{1}{L}\int_0^{L}\tau_w\,\mathrm{d}x=\tau_w ,$$ and dividing by the dynamic pressure formed on the exit velocity U0 = AL1/3 gives $$\boxed{\overline{C_f}=\frac{1.398}{\sqrt{\mathrm{Re}_L}},\qquad \mathrm{Re}_L=\frac{AL^{4/3}}{\nu}}$$ i.e. the average coefficient is numerically equal to the local coefficient evaluated at x = L. On a flat plate the average is 2 times the trailing-edge local value; here the ratio is exactly 1, which is a compact way of stating the same uniform-shear result.
  10. Put numbers on it. For air (ρ = 1.2 kg/m3, ν = 1.5 × 10−5 m2/s) with A = 5 SI units and a 1.0 m test length, the exit velocity is 5.0 m/s, ReL = 3.33 × 105, δ(L) = 4.95 mm, Cfx(L) = 2.42 × 10−3 and τw = 0.0363 Pa. Recomputing the shear directly from the profile, 2μU0/δ = 2(1.8 × 10−5)(5.0)/0.00495, returns the same 0.0363 Pa, and evaluating it at x = 0.2 m and x = 2.5 m returns 0.0363 Pa there too — the uniformity claimed in step 8.
Check: the question labels δ* and θ as “the momentum and displacement thickness, respectively”, which transposes the two names. Integrating the printed parabolic profile gives ∫(1 − u/U0)d(y/δ) = 1/3, the displacement thickness, and ∫(u/U0)(1 − u/U0)d(y/δ) = 2/15, the momentum thickness — so the printed ratios are correct and only the two words are swapped. The solution uses δ*/δ = 1/3 as the displacement thickness and θ/δ = 2/15 as the momentum thickness, which is what the momentum-integral equation requires. The shape factor H = δ*/θ = 2.5 is the standard value for a parabolic profile, confirming the assignment.
PartQuantityResult
(a)Growth exponentn = 1/3 (with B = √(90ν/11A))
(b)Relative thicknessδ/x = √(90/11 Rex) = 2.860 Rex−1/2
(c)Local skin frictionCfx = 1.398 Rex−1/2
(d)Average skin frictionC̄f = 1.398 ReL−1/2 (equal to the local value at x = L)
—Wall shear stressτw = 0.699 ρA3/2ν1/2, constant along the tunnel
—Worked illustration (A = 5, L = 1 m, air)δ(L) = 4.95 mm, Cfx(L) = 2.42 × 10−3, τw = 0.0363 Pa
Back to the paper →