22-Mec-B2 Environmental Control in Buildings · May 2017
Question 7 of 8: Round duct sizing by the equal-friction method
Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)
Notes on this paper
Paper format. Professional Engineers of
Ontario / Engineers Canada annual examination 16-Mec-B2 Environmental
Control in Buildings, May 2017, three hours, open book.
Eight problems of 20 points each; candidates are required to solve five, and all
questions carry the same value. ASHRAE psychrometric charts (SI and inch-pound)
and an R-717 pressure–enthalpy diagram are appended to the paper.
All eight problems are solved here.
Reference texts for this subject.
W. P. Jones, Air Conditioning Engineering, 5th ed.,
Butterworth-Heinemann — the standard reference for this examination
code; Ch. 2–3 (psychrometry and the psychrometric chart), Ch. 6
(air-conditioning plant cycles), Ch. 9 (cooling towers), Ch. 15 (fans and
duct design).
McQuiston, Parker & Spitler, Heating, Ventilating and Air
Conditioning: Analysis and Design, 6th ed., Wiley — Ch. 3 (moist
air), Ch. 5 (heat transmission in building structures), Ch. 8 (energy
estimating and the degree-day method), Ch. 12–13 (fluid flow, fans and
duct design).
ASHRAE Handbook — Fundamentals (2021) — Ch. 1
(psychrometrics), Ch. 14 (climatic design information), Ch. 18
(non-residential cooling and heating load calculations), Ch. 21 (duct
design), Ch. 25–27 (thermal and moisture performance of the building
envelope).
Çengel & Boles, Thermodynamics: An Engineering Approach,
9th ed., McGraw-Hill — Ch. 11 (refrigeration cycles, including
multistage compression with a flash chamber) and Ch. 14 (gas–vapour
mixtures and air conditioning).
National Energy Code of Canada for Buildings (NECB 2020) and CSA
F280 — the Canadian regulatory frame for envelope U-factors
and heating-load calculation.
Conventions used throughout. Moist-air properties are
computed from the ASHRAE Handbook — Fundamentals Ch. 1 formulation at a
barometric pressure of 101.325 kPa, so that every state point can be checked
against the charts appended to the paper. Enthalpy is referred to dry air at
$0^{\circ}\text{C}$ and liquid water at $0^{\circ}\text{C}$, i.e.
$h = 1.006\,t + W\,(2501 + 1.86\,t)$ in kJ per kilogram of dry air. Problems 3
and 6 to 8 are worked in the inch-pound units in which they are set, as the
examination directs.
Question 7: Round duct sizing by the equal-friction method (20 marks)
Given. A small low-velocity supply system of three outlets
totalling 320 cfm, with the run lengths scaled from the figure and the terminal
pressure requirement marked at each outlet.
System data scaled from the figure, Problem 7
Section
Route
Flow, cfm
Length, ft
1
plenum to A
320
25
2
A to B
220
18
3
B to C
100
10
4
C to outlet 2 (8 ft rise + 25 ft run)
100
33
5
B down to outlet 3
120
18
6
riser at A to outlet 1
100
5 (assumed)
terminal losses: outlet 1, 0.050 in wg; outlet 2, 0.040 in wg; outlet 3, 0.035 in wg. Total pressure available at the plenum 0.15 in wg.
Find. A round duct size for every section, the resulting
pressure balance on each of the three runs, and the damper settings needed to
balance the system.
Assumptions stated (the question asks for them
explicitly):
Galvanised steel round duct, absolute roughness
$\varepsilon = 0.0003$ ft (ASHRAE "medium smooth"), carrying standard air at
$0.075\ \text{lb}/\text{ft}^{3}$.
The lengths marked on the figure are taken as total equivalent
lengths, i.e. the equivalent lengths of the elbows, take-offs and
transitions are already included. If instead fittings were added at the
customary 50 % of measured length, the design friction rate would fall from
0.128 to 0.085 in wg per 100 ft and every duct would come out one nominal size
larger.
The riser at A is not dimensioned on the figure; 5 ft is allowed for it.
Because that run is not the index run, the assumption affects only the damper
setting at outlet 1.
The pressure quoted at each outlet is the total pressure the diffuser and
its neck require; the plenum pressure of 0.15 in wg is total pressure, so
velocity-pressure regain is not credited — conservative for a system this
small.
Duct sizes are selected from the standard round series (4, 5, 6, 7, 8, 9,
10, 12 in), rounding up from the calculated diameter.
Approach. Identify the index run — the one that
consumes the most pressure — and spend the available pressure on it:
subtract its terminal loss, divide what remains by its total equivalent length
to get a friction rate, then size every section of the system at that same
rate. Finally re-total each run at the selected sizes and damper off the
surplus at the two short outlets.
Total the flows and find the index run. The three outlets
draw $100+100+120=320$ cfm. Three routes leave the plenum, and their duct
lengths are 30 ft to outlet 1, $25+18+10+33=86$ ft to outlet 2, and
$25+18+18=61$ ft to outlet 3. Outlet 2 is both the longest and carries the
second-largest terminal loss, so it is the index run.
Set the design friction rate. Of the 0.15 in wg available,
the index outlet's diffuser takes 0.040, leaving 0.110 in wg to be spent on
86 ft of duct:
$$\text{friction rate}=\frac{0.150-0.040}{86}\times100
=\boxed{0.128\ \text{in wg per 100 ft}}$$
This is a normal low-pressure design rate; the customary band is 0.08 to
0.15 in wg per 100 ft for commercial supply ductwork, chosen to keep
velocities and hence noise down.
Size each section at that rate. For round duct the
friction loss per 100 ft is
$$\frac{\Delta p}{100\ \text{ft}}=f\,\frac{100}{D}\left(\frac{V}{4005}\right)^{2}$$
with $f$ from the Colebrook equation,
$1/\sqrt{f}=-2\log_{10}\!\left[\varepsilon/3.7D+2.51/(Re\sqrt{f})\right]$, $D$
in feet and $V$ in feet per minute. Solving for the diameter that gives 0.128
in wg per 100 ft at each flow, and rounding up to the standard series:
Tabulate the selection. The required and selected
diameters, with the velocity and the actual loss at the selected size:
Duct selection at 0.128 in wg per 100 ft
Section
cfm
Calculated $D$, in
Selected $D$, in
Velocity, fpm
Loss per 100 ft
Section loss, in wg
1 plenum–A
320
8.46
9
724
0.0945
0.0236
2 A–B
220
7.36
8
630
0.0848
0.0153
3 B–C
100
5.48
6
509
0.0825
0.0083
4 C–outlet 2
100
5.48
6
509
0.0825
0.0272
5 B–outlet 3
120
5.87
6
611
0.1147
0.0207
6 riser at A
100
5.48
6
509
0.0825
0.0041
Every velocity is between 500 and 730 fpm, well inside the 600–1000 fpm
band that keeps a small office system quiet, so no size needs to be revisited
for noise.
Total each run and check the index. Adding the section
losses along each route and adding the terminal loss:
$$\text{outlet 2 (index)}:\ 0.0236+0.0153+0.0083+0.0272+0.040=\boxed{0.114\ \text{in wg}}$$
$$\text{outlet 3}:\ 0.0236+0.0153+0.0207+0.035=0.095\ \text{in wg}$$
$$\text{outlet 1}:\ 0.0236+0.0041+0.050=0.078\ \text{in wg}$$
The index run needs 0.114 in wg against the 0.15 available, so the system
works, with 0.036 in wg in hand — the margin arises because every duct
was rounded up to the next standard size, which is exactly why one
rounds that way.
Balance the system. The two short runs must be throttled
to the same total, or all the air will short-circuit to them:
$$\text{damper at outlet 1}:\ 0.150-0.078=0.072\ \text{in wg}$$
$$\text{damper at outlet 3}:\ 0.150-0.095=0.055\ \text{in wg}$$
Volume dampers are therefore required at both take-offs, and are needed even in
a system as small as this because the pressure to be absorbed at outlet 1 is
nearly half the total available. Proportional balancing against measured flows
is the commissioning step that finally sets them.
Sanity-check the result. A useful cross-check on any
equal-friction design is that the main should be roughly one nominal size above
the sum of the branches it serves: 9 in for 320 cfm, 8 in for 220 cfm and 6 in
for 100–120 cfm follow the expected progression, and the fan needs only
$0.15\ \text{in wg}\times320\ \text{cfm}/(6356\times0.55)\approx0.014$ hp of
air power — a fractional-horsepower fan, consistent with a small
terminal system.
Check: the answer depends on how fittings are
treated, and this is the assumption to declare. Reading the marked
lengths as total equivalent lengths gives 0.128 in wg per 100 ft and the sizes
tabulated above. Adding a conventional 50 % allowance for the two elbows, three
take-offs and the plenum entry would give 129 ft of equivalent length on the
index run and a rate of 0.085 in wg per 100 ft, moving sections 1, 2 and 5 up
one nominal size (10, 9 and 7 in). Either answer is defensible provided the
assumption is stated, which the question explicitly requires.
The system with the selected round sizes marked. Nodes A,
B and C are the three take-off points; the index run is plenum–A–B
–C–outlet 2, 86 ft of duct plus a 0.040 in wg diffuser.
Problem 7 — results
Quantity
Value
Total system flow
320 cfm
Index run
plenum–A–B–C–outlet 2, 86 ft equivalent
Design friction rate
0.128 in wg per 100 ft
Selected sizes, sections 1 to 6
9, 8, 6, 6, 6, 6 in diameter
Velocities
509 to 724 fpm (all within the low-noise band)
Run totals (duct + terminal)
outlet 1, 0.078; outlet 2, 0.114; outlet 3, 0.095 in wg
Balancing dampers
outlet 1, absorb 0.072 in wg; outlet 3, absorb 0.055 in wg