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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.

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)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

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
SectionRouteFlow, cfmLength, ft
1plenum to A32025
2A to B22018
3B to C10010
4C to outlet 2 (8 ft rise + 25 ft run)10033
5B down to outlet 312018
6riser at A to outlet 11005 (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):

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.

  1. 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.
  2. 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.
  3. 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:
  4. 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
    SectioncfmCalculated $D$, inSelected $D$, inVelocity, fpmLoss per 100 ftSection loss, in wg
    1 plenum–A3208.4697240.09450.0236
    2 A–B2207.3686300.08480.0153
    3 B–C1005.4865090.08250.0083
    4 C–outlet 21005.4865090.08250.0272
    5 B–outlet 31205.8766110.11470.0207
    6 riser at A1005.4865090.08250.0041
    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.
  5. 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.
  6. 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.
  7. 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.

plenum 100 cfm outlet 1, 0.050 in wg 100 cfm outlet 2, 0.040 in wg 120 cfm outlet 3, 0.035 in wg 25 ft · 9 in 18 ft · 8 in 10 ft 6 in 8 + 25 ft · 6 in 18 ft · 6 in 5 ft · 6 in A B C 0.15 in wg total pressure available at the plenum; index run plenum-A-B-C-outlet 2 (86 ft)
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
QuantityValue
Total system flow320 cfm
Index runplenum–A–B–C–outlet 2, 86 ft equivalent
Design friction rate0.128 in wg per 100 ft
Selected sizes, sections 1 to 69, 8, 6, 6, 6, 6 in diameter
Velocities509 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 dampersoutlet 1, absorb 0.072 in wg; outlet 3, absorb 0.055 in wg
Spare pressure on the index run0.036 in wg