22-Mec-B2 Environmental Control in Buildings · December 2019
Question 8 of 8: Duct sizing for equal branch friction, and the effect of hot low-pressure air
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. National Examinations, December 2019 — 16-Mec-B2 Environmental
Control in Buildings. Three hours, open book: only textbooks and reference books are permitted
(no notes and no solved problems), any non-communicating calculator is allowed, and candidates are
expected to bring both an environmental-control text and steam tables because the tables and graphs
in those books are needed. Eight problems are printed at 20 points each and only the first
five in the exam book are graded, so the printed paper totals 160 points and a graded script
totals 100. Psychrometric charts (IP and SI) and an R-134a pressure–enthalpy diagram are
attached as the last three pages. All eight problems are worked below.
McQuiston, Parker & Spitler, Heating, Ventilating and Air Conditioning: Analysis and
Design, 6th ed. — plant psychrometry, duct design, infiltration and the degree-day method.
Jones, Air Conditioning Engineering, 5th ed. — percentage saturation, cooling-tower
analysis, apparatus dew point and coil by-pass factor.
Çengel & Ghajar, Heat and Mass Transfer, 6th ed., Ch. 3 —
one-dimensional composite walls and thermal bridging; Table A-5 for building-material
conductivities.
Stoecker & Jones, Refrigeration and Air Conditioning, 2nd ed. — vapour-compression
cycles and heat pumps; ASHRAE Refrigerant Tables for R-134a on the datum of the attached
chart (hf = sf = 0 at −40 °F).
Eastop & McConkey, Applied Thermodynamics for Engineering Technologists, 5th ed.
— the SI cooling-tower mass/energy balance in the form this paper uses.
Canadian context: ASHRAE Standard 170 Ventilation of Health Care
Facilities (adopted by CSA Z317.2 for Canadian hospitals); Health Canada
Residential Indoor Air Quality Guidelines; National Building Code of Canada 9.36 and the
National Energy Code of Canada for Buildings (NECB 2020); Environment and Climate Change Canada
Canadian Climate Normals for degree-day and design-temperature data.
Check — assumptions declared under cover-page instruction 1
Cover-page instruction 1 asks candidates to state any interpretive assumption with the answer.
Four are needed on this paper and each is flagged again where it is used: the operating-room
dry-bulb temperature in Problem 1 (not given — taken as
75 °F, the top of the ASHRAE 170 range, because it is the
only part of that range that also satisfies the 60 % relative-humidity ceiling); the
Winnipeg design conditions and degree-day base in Problem 6 (the paper says
“select the design conditions”); the indoor design temperature and neutral pressure
level in Problem 7(b); and the duct roughness and fitting allowance in
Problem 8. Everything else in the paper is fully determined by the data given.
Question 8: Duct sizing for equal branch friction, and the effect of hot low-pressure air
(20 marks)
Main duct, 25 ft + 6 ft from the fan to the junction
—
40 in × 24 in, 12 000 cfm
Branch A
—
6 000 cfm, 100 ft
Branch B
—
4 000 cfm, 150 ft
Branch C
—
2 000 cfm, 35 ft
Target friction loss per branch
Δpf
0.15 in. wg
Velocity limit
Vmax
2 000 fpm
Part (b) air state
—
150 °F, 14.0 psia, same 12 000 cfm
Find. A round-duct size for each branch that produces the same 0.15 in. wg
of friction without exceeding 2 000 fpm; the total friction loss of the same volumetric flow
of hot, low-pressure air through the same ducts; and the fan speed needed to deliver it.
Figure 8.1 — the duct system read from the
paper's own sketch: 25 ft of 40 in × 24 in main from the fan, a
transition, 6 ft more to the junction, then branch A rising 100 ft, branch B continuing
150 ft and branch C dropping 35 ft.
Approach. Convert each branch's 0.15 in. wg total loss into a
friction rate per 100 ft, solve the Darcy–Weisbach equation with Colebrook–White
friction for the diameter at that rate, then check each result against the velocity limit and enlarge
where it governs. For part (b) recompute the same ducts at the hot-air density and viscosity; for part
(c) apply the fan laws.
Part (a) — turn the equal-total-loss requirement into a friction rate for each
branch. Equal total loss over unequal lengths means unequal loss per unit length:
$$\text{A:}\ \frac{0.15}{100}\times 100 = 0.150,\qquad
\text{B:}\ \frac{0.15}{150}\times 100 = 0.100,\qquad
\text{C:}\ \frac{0.15}{35}\times 100 = 0.429\ \text{in.\ wg per 100 ft}$$
This is a balanced-pressure-loss design rather than the constant-friction-rate method: because the
branches all discharge from one junction, making their losses equal is what makes the system
self-balancing without dampers.
Solve for each diameter from Darcy–Weisbach. With
$$\Delta p_f = f\,\frac{L}{D}\,\frac{\rho V^2}{2}, \qquad
\frac{1}{\sqrt f} = -2\log_{10}\!\left(\frac{\varepsilon}{3.7D} + \frac{2.51}{Re\sqrt f}\right)$$
at ρ = 0.0749 lb/ft³ and the ASHRAE friction-chart roughness
for galvanised steel ε = 0.0003 ft (0.09 mm), the required
diameters are
$$D_A = 24.7\ \text{in} \;(V = 1\,799\ \text{fpm}), \qquad
D_B = 23.0\ \text{in} \;(V = 1\,384\ \text{fpm}), \qquad
D_C = 13.2\ \text{in} \;(V = 2\,100\ \text{fpm})$$
Branch A and branch B satisfy the velocity limit, but branch C does not — and
that is the reason the limit is stated in the question.
Enlarge branch C until the velocity limit is met. The smallest duct that keeps
2 000 cfm at or below 2 000 fpm needs
A = 1.00 ft², so
$$D_C = \sqrt{\frac{4 \times 1.00}{\pi}} \times 12 = \boxed{13.5\ \text{in}}
\qquad (V = 2\,000\ \text{fpm exactly})$$
At that size branch C loses only 0.133 in. wg rather than 0.150, so it is now the
least resistant path and will take more than its share of air unless a balancing damper adds
back the missing 0.017 in. wg. Reporting that damper requirement is part of the answer: the
velocity constraint has broken the self-balancing property the equal-friction design was chosen
for.
Give the practical selections. Ducts are made in standard sizes, so the design
sizes round up to the next available diameter, and the actual losses follow:
Branch
cfm
Length
Required D
Selected
Actual V
Actual loss
A
6 000
100 ft
24.7 in
26 in ø
1 627 fpm
0.117 in. wg
B
4 000
150 ft
23.0 in
24 in ø
1 273 fpm
0.122 in. wg
C
2 000
35 ft
13.5 in
14 in ø
1 871 fpm
0.113 in. wg
Rectangular equivalents follow from
De = 1.30(ab)0.625/(a+b)0.25 if the
installation needs flat ducts. The selected sizes happen to land within 8 % of one another in loss,
which is as close to balanced as standard sizes allow.
Add the main run to get the fan's duty. The 40 in × 24 in
main has a face area of 6.667 ft², so
V = 12 000/6.667 = 1 800 fpm (within the limit), and its
circular equivalent is
$$D_e = 1.30\,\frac{(40 \times 24)^{0.625}}{(40 + 24)^{0.25}} = 33.6\ \text{in}$$
Over the 25 ft + 6 ft = 31 ft to the junction it loses 0.037 in. wg, so the
index (longest-resistance) run totals
$$\Delta p_{total,(a)} = 0.037 + 0.150 = \boxed{0.188\ \text{in.\ wg}}$$
This is friction only: no loss coefficients are given for the fan-outlet transition, the tee or the
grilles, and a real selection would add 0.2 to 0.4 in. wg of fitting and terminal
losses.
Part (b) — fix the hot-air properties. At 150 °F and 14.0 psia,
$$\rho_h = \frac{14.0 \times 144}{53.35 \times 609.67} = 0.0620\ \text{lb/ft}^3
\quad\left(\frac{\rho_h}{\rho_s} = 0.828\right), \qquad
\frac{\mu_h}{\mu_s} = 1.113$$
Because the volumetric flow is unchanged, every velocity in the system is unchanged; only the density
and viscosity move.
Recompute the losses. Friction loss is proportional to density at a given velocity,
but the Reynolds number falls by the ratio
(ρh/ρs)(μs/μh) =
0.744, so the friction factor rises a little and the loss does not fall quite in proportion to
density:
$$\Delta p_{total,(b)} = 0.032\ (\text{main}) + 0.129\ (\text{branch B, now the index run})
= \boxed{0.161\ \text{in.\ wg}}$$
That is 0.861 times the design value, against the 0.828 that a pure density scaling would predict. The
4.0 % difference is the viscosity effect, and it is smaller than the accuracy with which the
friction chart can be read — so the practical answer is
0.188 × 0.828 = 0.155 in. wg, and the exact figure is
0.161.
Part (c) — the fan speed. The fan laws at constant size give
Ṁ ∝ N,
Δp ∝ ρN² and
P ∝ ρN³. The requirement is the same 12 000 cfm, and
flow depends on speed alone, so
$$\frac{\dot V_2}{\dot V_1} = \frac{N_2}{N_1} = 1
\quad\Longrightarrow\quad \boxed{N_2 = 100\ \%\ \text{of the part-(a) speed}}$$
and the consistency of that answer is the point of the question: at unchanged speed the fan's
pressure falls to
0.188 × 0.828 = 0.155 in. wg and the system's requirement
falls to almost exactly the same figure, because both scale with density. A fan is a
constant-volume machine; hot air does not change what it can move, only the pressure it develops and
the power it draws. Its shaft power falls by the same density ratio, to 82.8 % of the design value
— which is why a fan sized on hot air can overload its motor if the system is ever started
cold.
State the second-order correction honestly. Carrying the friction-factor change
from step 7, the system needs 0.161 rather than 0.155 in. wg, a 3.7 % shortfall that
would take
√1.037 = 1.018, or about 102 % speed, to make up.
The first-order answer of 100 % is the one the fan laws give and the one the question is
testing; the 2 % is well inside the tolerance of a fan curve and of the friction chart, and is
reported rather than carried.
Quantity
Symbol
Result
Branch A size (part a)
DA
24.7 in ø (select 26 in); 1 799 fpm; friction-governed
Branch B size (part a)
DB
23.0 in ø (select 24 in); 1 384 fpm; friction-governed
Branch C size (part a)
DC
13.5 in ø (select 14 in); 2 000 fpm; velocity-governed
Branch C loss and balancing damper
—
0.133 in. wg; damper to add 0.017 in. wg
Main duct: equivalent diameter, velocity, loss
De
33.6 in; 1 800 fpm; 0.037 in. wg over 31 ft
System total, standard air (index run)
Δp(a)
0.188 in. wg (friction only)
Hot-air density / viscosity ratio
—
0.828 × / 1.113 ×
Total friction loss at 150 °F, 14.0 psia (part b)
Δp(b)
0.161 in. wg (0.155 by pure density scaling)
Fan speed required (part c)
N2/N1
100 % by the fan laws (102 % if the friction-factor shift is carried)