22-Mec-B6 Advanced Fluid Mechanics · Undated paper
Question 3 of 6: Forces on the flange of a curved discharge pipe
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Exams, May 2019 —
printed code 16-Mec-A6Advanced Fluid Mechanics (the cover page and every running header read 16-Mec-A6, May 2019). Three hours, OPEN BOOK, any approved Sharp or Casio calculator permitted. Six questions are printed; any five of them constitute a complete paper for 100 marks, each question carries an equal 20 marks, and the item weights are printed 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 from 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. — control-volume momentum (§3.4),
potential-flow building blocks (§4.4, §8.2–8.3), dimensional analysis and
modelling (§5.2–5.4), turbulent flat-plate layers (§7.4), isentropic and
normal-shock relations (§9.3–9.5).
J. D. Anderson, Modern Compressible Flow, 3rd ed. — quasi-one-dimensional
nozzle flow and normal shocks (Ch. 3 and Ch. 5).
F. M. White, Viscous Fluid Flow, 3rd ed. — exact solutions of the
Navier–Stokes equations (§3.2).
P. K. Kundu, I. M. Cohen & D. R. Dowling, Fluid Mechanics, 6th ed. —
complex potential and plane potential flows (Ch. 6); boundary layers (Ch. 9).
R. W. Fox, A. T. McDonald & J. W. Mitchell, Introduction to Fluid Mechanics,
10th ed. — momentum analysis of pipe bends (Ch. 4) and similitude (Ch. 7).
SI units throughout. Air and mercury properties are those printed in the question; all pressures
are absolute unless a gauge value is stated explicitly. Water and air properties not printed in the
paper are taken from the standard Canadian-edition property tables at the stated temperatures, and
each such value is named where it is used.
Question 3: Forces on the flange of a curved discharge pipe (20 marks)
Find. The $x$ and $y$ components of the force the flange must carry, together with
the magnitude and direction of their resultant.
[Figure not reproduced: Figure 3 (redrawn). The flanged bend, its control volume (shaded) and the resultant load the pipe transmits to the flange bolts — 154.9 N acting 21.7° below the inlet flow direction. See the official exam paper.]
Approach. Take a control volume that cuts the pipe at the flange and encloses the
whole bend; get the inlet gauge pressure from Bernoulli between the inlet section and the free jet;
then apply the steady linear-momentum equation in $x$ and $y$, with the flange reaction as the only
unknown.
Compute the two section velocities from continuity.
$$A_1 = \frac{\pi D^{2}}{4} = \frac{\pi (0.100)^2}{4} = 7.854\times10^{-3}\;\text{m}^2,
\qquad A_2 = \frac{\pi d^{2}}{4} = 1.963\times10^{-3}\;\text{m}^2$$
$$V_1 = \frac{Q}{A_1} = \frac{0.0150}{7.854\times10^{-3}} = 1.910\;\text{m/s},
\qquad V_2 = \frac{Q}{A_2} = \frac{0.0150}{1.963\times10^{-3}} = 7.639\;\text{m/s}$$
The velocity ratio is $(D/d)^2 = 4.00$ exactly, which is a free arithmetic check on both numbers.
The mass flow is $\dot m = \rho Q = 998 \times 0.0150 = 14.97\;\text{kg/s}$.
Find the inlet gauge pressure from Bernoulli. With friction and elevation
neglected as instructed and the exit a free jet at atmospheric pressure ($p_2 = 0$ gauge),
$$p_1 + \tfrac{1}{2}\rho V_1^{2} = p_2 + \tfrac{1}{2}\rho V_2^{2}
\quad\Longrightarrow\quad p_1 = \tfrac{1}{2}\rho\left(V_2^{2}-V_1^{2}\right)$$
$$p_1 = \tfrac{1}{2}(998)\left(58.36 - 3.648\right) = \boxed{27.30\;\text{kPa gauge}}$$
This pressure acts over the full inlet area and, as step 4 shows, it dominates the answer.
Set up the momentum balance. Let $x$ point along the inlet flow and $y$ vertically
upward, and let $\mathbf{F}_R = (F_{Rx}, F_{Ry})$ be the force the flange exerts on the
control volume. Only the inlet pressure force and the flange reaction act on the CV, because the
outside of the bend and the exit jet are both at atmospheric pressure and gravity is neglected. For
steady flow with uniform profiles,
$$\sum F_x = \dot m\left(V_2\cos\alpha - V_1\right),\qquad
\sum F_y = \dot m\left(V_2\sin\alpha - 0\right)$$
Solve the $x$ component. The pressure force at the inlet is
$p_1 A_1 = 27\,302 \times 7.854\times10^{-3} = 214.4\;\text{N}$ in the $+x$ direction, so
$$F_{Rx} + p_1A_1 = \dot m\left(V_2\cos 30^\circ - V_1\right)$$
$$F_{Rx} = 14.97\,(6.615 - 1.910) - 214.4 = 70.4 - 214.4 = \boxed{-144.0\;\text{N}}$$
The negative sign says the flange must pull the bend backwards, against the incoming flow.
That is physically right: the jet leaving at 7.64 m/s carries away far less $x$-momentum flux
(70.4 N of change) than the 214.4 N the inlet pressure pushes forward, so the bolts must
absorb the difference.
Solve the $y$ component. No pressure force has a $y$ component, so the flange
supplies the entire vertical momentum change:
$$F_{Ry} = \dot m\,V_2\sin 30^\circ = 14.97 \times 7.639 \times 0.5000 = \boxed{+57.2\;\text{N}}$$
Assemble the resultant and reverse it onto the flange. The force of the flange on
the pipe is $\mathbf{F}_R = (-144.0,\;+57.2)\;\text{N}$, of magnitude
$$|\mathbf{F}_R| = \sqrt{144.0^{2}+57.2^{2}} = 154.9\;\text{N}$$
at $\arctan(57.2/144.0) = 21.7^\circ$ above the $-x$ axis, i.e. 158.3° measured from $+x$. By
Newton’s third law the bend transmits the equal and opposite load to the flange:
$$\boxed{\mathbf{F}_{\text{on flange}} = (+144.0\,\hat{\mathbf{i}} - 57.2\,\hat{\mathbf{j}})\;\text{N},
\qquad |\mathbf{F}| = 154.9\;\text{N} \text{ at } 21.7^\circ \text{ below } +x}$$
The bolts are therefore loaded in tension along the pipe axis and in shear vertically, which is the
practical conclusion a designer needs.
Quantity
Result
Inlet velocity $V_1$
1.910 m/s
Exit velocity $V_2$
7.639 m/s
Mass flow $\dot m$
14.97 kg/s
Inlet gauge pressure $p_1$
27.30 kPa
Inlet pressure force $p_1A_1$
214.4 N
Flange reaction on the pipe, $F_{Rx}$
−144.0 N (opposing the flow)
Flange reaction on the pipe, $F_{Ry}$
+57.2 N (upward)
Resultant magnitude and direction
154.9 N at 158.3° from $+x$ (on the pipe); 21.7° below $+x$ on the flange
Check: water density is taken as
$\rho = 998\;\text{kg/m}^3$ (fresh water near 20 °C), since the paper does not print it.
Using 1000 kg/m³ instead changes every force by +0.2 % — $F_{Rx} = -144.2\;\text{N}$,
$|\mathbf{F}| = 155.2\;\text{N}$ — which is far inside the “estimate” the question
asks for.