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:
F. M. White, Fluid Mechanics, 8th ed. — potential-flow building blocks
(§4.4, §8.2–8.3), rigid-body motion of a fluid (§2.9), flow in
non-circular ducts and minor losses (§6.6–6.7), dimensional analysis
(§5.2–5.4), the momentum integral (§7.4), compressible nozzle flow and normal
shocks (§9.4–9.6).
F. M. White, Viscous Fluid Flow, 3rd ed. — exact Navier–Stokes solutions in
cylindrical coordinates (§3.2–3.4) and integral boundary-layer methods
(§4.5).
J. D. Anderson, Modern Compressible Flow, 3rd ed. — quasi-one-dimensional nozzle
flow, choking and normal shocks (Ch. 3, §3.3 and §3.6).
P. K. Kundu, I. M. Cohen & D. R. Dowling, Fluid Mechanics, 6th ed. — the
complex potential and elementary singularities (Ch. 6); boundary layers (Ch. 9).
H. Schlichting & K. Gersten, Boundary-Layer Theory, 9th ed. —
Kármán–Pohlhausen integral method for accelerating external flows
(Ch. 8).
R. W. Fox, A. T. McDonald & J. W. Mitchell, Introduction to Fluid Mechanics,
10th ed. — the repeating-variable procedure and pipe-system energy accounting
(Ch. 7, Ch. 8).
Question 6: Boundary layer in an accelerating suction wind tunnel (20 marks)
parabolic, satisfies u = U0 and ∂u/∂y = 0 at y = δ
Displacement thickness
δ*/δ = 1/3
from ∫(1 − u/U0)dy
Momentum thickness
θ/δ = 2/15
from ∫(u/U0)(1 − u/U0)dy
Assumed growth law
δ = B xn
with δ = 0 at x = 0
Regime
two-dimensional, laminar, constant properties
ν = 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.
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.
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.
Evaluate the wall shear from the assumed profile. Differentiating
$u/U_0=2(y/\delta)-(y/\delta)^{2}$ at the wall,
$$\tau_w=\mu\left.\frac{\partial u}{\partial y}\right|_{y=0}=\frac{2\mu U_0}{\delta}
\quad\Longrightarrow\quad \frac{\tau_w}{\rho U_0^{2}}=\frac{2\nu}{U_0\delta}.$$
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
$$\frac{2\nu}{U_0\delta}=\frac{2\nu}{AB}x^{-m-n}.$$
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.
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
$$\boxed{B=\sqrt{\frac{90\,\nu}{11\,A}}}$$
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.
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).
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.
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.
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.
Part
Quantity
Result
(a)
Growth exponent
n = 1/3 (with B = √(90ν/11A))
(b)
Relative thickness
δ/x = √(90/11 Rex) = 2.860 Rex−1/2
(c)
Local skin friction
Cfx = 1.398 Rex−1/2
(d)
Average skin friction
C̄f = 1.398 ReL−1/2 (equal to the local value at x = L)
—
Wall shear stress
τw = 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