Question 3 of 6: Net force of the pipe on the fluid in a choked adiabatic duct
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Exams, May 2016 —
07-Mec-B6 Advanced Fluid Mechanics. Three hours, OPEN BOOK, any
approved Sharp or Casio calculator permitted. Six questions are printed; any five
of them constitute a complete paper, each carries an equal 20 marks, and the item weights
are shown in the left margin. No aid sheet is bound into this 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. 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), laminar boundary layers and the momentum integral
(§7.2–7.4), dimensional analysis (§5.2–5.4), compressible duct
flow (§9.5–9.7).
F. M. White, Viscous Fluid Flow, 3rd ed. — exact solutions of the
Navier–Stokes equations 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, normal shocks and Fanno flow (Ch. 3, Ch. 5).
P. K. Kundu, I. M. Cohen & D. R. Dowling, Fluid Mechanics, 6th ed. —
complex potential, images and the Blasius/Lagally force theorems (Ch. 6); boundary
layers (Ch. 9).
B. R. Munson et al., Fundamentals of Fluid Mechanics, 8th ed. —
Buckingham Pi method and the repeating-variable procedure (Ch. 7).
Question 3: Net force of the pipe on the fluid in a choked adiabatic duct (20 marks)
Find. The net axial force the pipe exerts on the fluid — that is,
the resultant of the wall shear and any pressure the wall carries, taken as a single reaction
on the gas.
[Figure not reproduced: Figure 3 (redrawn) as a control volume. Because the area is constant and the duct is insulated, the flow follows the Fanno line; the integrated wall shear is the single unknown in the axial momentum balance, so neither the friction factor nor the duct length is needed. See the official exam paper.]
Approach. Get the inlet Mach number, use the Fanno relations to
find the sonic (exit) state, then close an axial momentum balance on the whole duct. The
force is what makes the balance balance, so it comes out without ever computing the friction
factor or the length.
Inlet Mach number. The speed of sound at the inlet is
$$a_{1}=\sqrt{\gamma R T_{1}}=\sqrt{1.4(287)(333.15)}=365.9\ \text{m/s},$$
so
$$M_{1}=\frac{V_{1}}{a_{1}}=\frac{110}{365.9}=0.301 .$$
The value is essentially exactly 0.30, which is the usual sign that this paper was built
backwards from a table entry — a helpful check that nothing has been misread.
Fanno ratios at the inlet. For adiabatic constant-area flow the sonic
reference state satisfies
$$\frac{T}{T^{*}}=\frac{\gamma+1}{2+(\gamma-1)M^{2}},\qquad
\frac{P}{P^{*}}=\frac{1}{M}\sqrt{\frac{T}{T^{*}}} .$$
At M1 = 0.301,
$$\frac{T_{1}}{T^{*}}=\frac{2.4}{2+0.4(0.301)^{2}}=1.1787,\qquad
\frac{P_{1}}{P^{*}}=\frac{1}{0.301}\sqrt{1.1787}=3.611 .$$
The exit (sonic) state. Because the duct is choked at the exit, station 2
is the sonic reference state:
$$T^{*}=\frac{333.15}{1.1787}=282.6\ \text{K},\qquad
P^{*}=\frac{680}{3.611}=188.3\ \text{kPa},$$
$$V^{*}=a^{*}=\sqrt{1.4(287)(282.6)}=337.0\ \text{m/s}.$$
Friction has cut the static pressure to 28 per cent of its inlet value while tripling the
velocity — the characteristic behaviour of a subsonic Fanno flow.
Mass flow, and a free continuity check. The inlet density is
$$\rho_{1}=\frac{P_{1}}{RT_{1}}=\frac{680\,000}{287(333.15)}=7.112\ \text{kg/m}^{3},$$
so
$$\dot m=\rho_{1}AV_{1}=7.112(0.013273)(110)=10.38\ \text{kg/s}.$$
Recomputing at the exit, ρ* = 188 300/[287(282.6)] = 2.321 kg/m3
and ρ*AV* = 10.38 kg/s — identical, which confirms
both end states at once. The stagnation temperature is likewise conserved,
T1(1 + 0.2M12) = 1.2T* =
339.2 K, as an insulated duct requires.
Axial momentum balance on the whole duct. Taking x along the
flow and calling F the net force the pipe applies to the fluid,
$$P_{1}A-P^{*}A+F=\dot m\left(V^{*}-V_{1}\right).$$
Substituting,
$$\dot m\left(V^{*}-V_{1}\right)=10.38(337.0-110)=2356\ \text{N},$$
$$\left(P_{1}-P^{*}\right)A=(680-188.3)\times 10^{3}\times 0.013273=6527\ \text{N},$$
$$F=2356-6527=-4169\ \text{N}.$$
The pressure drop alone would accelerate the gas far more than it actually accelerates, and
the deficit is exactly what the wall absorbs:
$$\boxed{\;\left|F\right|=4.17\ \text{kN, directed opposite to the flow}\;}$$
Equivalently, the fluid pushes the pipe downstream with 4.17 kN — the load the duct
supports and anchors must carry.
Cross-check with the impulse function. Defining
I = PA + ṁV, the same balance reads F =
I2 − I1:
$$I_{1}=680\,000(0.013273)+10.38(110)=10\,168\ \text{N},$$
$$I_{2}=188\,300(0.013273)+10.38(337.0)=5999\ \text{N},$$
$$I_{2}-I_{1}=-4169\ \text{N}\ \checkmark$$
This second form is worth writing down because it makes the one classic sign error —
adding rather than subtracting the momentum flux — impossible to hide.
What the answer does not depend on. Neither the friction factor
nor the duct length appears anywhere above, because the integrated wall shear is the single
unknown that the momentum balance solves for. For interest, the Fanno function at the inlet is
$$\frac{fL^{*}}{D}=\frac{1-M_{1}^{2}}{\gamma M_{1}^{2}}+\frac{\gamma+1}{2\gamma}
\ln\!\frac{(\gamma+1)M_{1}^{2}}{2+(\gamma-1)M_{1}^{2}}=5.27,$$
so at a plausible f = 0.018 the implied length is L* = 38 m.
That number is a plausibility note only; changing f changes the length, never the
force.