topic6-4 duct calculations by chart - khon kaen university
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Data: 1. pipe line diagram 2.Qmain & all Qbranch (m3/s or cfm)
Topic6-4 Duct Calculations by Chart
Step 1. Select air velocity: Vmain (m/s or fpm) [cost, noise, install, mainten]building; Vmain 4 – 12 m/s (800 – 2400 fpm), Vbrance 2.5 – 10 m/s (500 – 2000 fpm)
Industrial; Vmain 12–25 m/s (2400 – 5000 fpm), Vbrance 10–20 m/s (2000 – 4000 fpm)
Step 2. Main ductGraph pL(Q,V,D) → Known (Q,V) -- find pL,D
Step 3. Branch ductsGraph pL(Q,V,D) → Known (Q,pL) – find D,V
Step 4. Conversion
round - ab ductsGraph D(a,b) →Select b(D) – find a
Pressure drop; straight circular duct
Pressure drop in straight ducts
2
2V
D
Lfp =
p = pressure drop, Paf = friction factor, f(Re,/D)L = length, mD = inside diameter (ID) of duct, m = roughness of tube surface, mV = velocity of fluid, m/s = density of fluid, kg/m3
Re = Reynolds number, VD/ = viscosity, Pas [ = / , m2/s]
1. Eck’s formula, 1973 f = [-2log{/(3.715D)+15/Re}]-2
Modified formula (explicit)
Colebrook’s formula, 1939 (implicit) Moody’s chart - turbulent flow f = [-2log{/(3.7D)+2.51/(Ref 0.5)}]-2
2. Smamee&Jain’s formula, 1976f = 0.25[log{/(3.7D)+5.74/Re0.9}]-2
3. Haaland’s formula, 1983f = [-1.8log{(/(3.7D))1.11+6.9/Re}]-2
Data: 1. pipe line diagram 2.Qmain & all Qbranch (m3/s)
Duct Calculations by equations
Step 1. Select air velocity: Vmain (m/s) [cost, noise, install, maintenance]building; Vmain 4 – 12 m/s, Vbrance 2.5 – 10 m/s
Industrial; Vmain 12–25 m/s, Vbrance 10–20 m/s
Step 2. Dmain (m) = (4Qmain/Vmain)0.5 → Dm(Q,V)
Step 3. fm = 0.25[log{/3.7D+5.74/Re0.9}]-2, Re = VD/
Air 20C; = 1.2041 kg/m3, = 18.178E-6 Pas, sheet metal = 15E-5 mfm = 0.25[log{1/(24667D)+1/(3802.7(VD)0.9)}]-2 → fm(V,D)
Step 4. pL (pa/m) = fmV2/(2D) = fmV2/(1.661D) → pL(f,V,D)
Step 5. Find fb for each branch Qb by solve implicit eq.fb = 0.25[log{(pL/fbQb
2)0.2/24547 +(fb/pLQb3)0.18/4747}]-2 → fb(f,Q,pL)
Step 6. Db = (fbQb2/(1.0246pL))
0.2 → Db(f,Q,pL)
Step 7. Vb = 4Qb/(Db2)→ Vb(D,Q) check for appropriate, noise etc.
Step 8. Deq,f = 1.265(ab)0.6/(a+b)0.2 → D(a,b)
SI unit:
D (m), V (m/s),
Q (m3/s), pL(Pa/m)
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Duct A
branch
elbow
Duct B 3 m3/s
Duct C
Ex1. A two-branch duct system of rectangular air duct with the duct height not greater than 40 cm. is shown. The fittings have the following equivalent length of straight duct: upstream to branch, 4 m; elbows, 2 m. There is negligible pressure loss in the straight-through section of the branch. The designer selects 10 m/s as the velocity in the duct section A. in the 12- and 15-m straight sections. What diameter and ab of duct A, B and C should be selected to use the available pressure without dampering (equal-friction method)? Show calculations and fill in the table.
1 m3/s
8 m
Data: 1. PLD
2.Qmain & all Qbranch
Step 1. Vmain = 10 m/s (large building)
Pressure drop in straight, circular, sheet-metal ducts, 20 C air, absolute roughness 0.00015 m.
Graph p/L & Q @D, V
Step 2.Known (Q, D) -- find p, V
QA = 4 m3/sVA = 10 m/s
pL = 1.4-1.5 Pa/m
DA = 0.7-0.72 m
Step 3.QB = 3 m3/sDB = 0.63-0.64 mVB = 9.2-9.4 m/s
Step 3.QC = 1 m3/sDC = 0.41-0.42 mVC = 7.1-7.2 m/s
Step 4.DA = 0.7 mbA = 40 cmaA = 110 cm
0.7-0.72 1.4-1.5
1.4-1.5
1.4-1.5
0.63-0.649.2-9.4
0.41-0.427.1-7.2
110
90
36
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Step 3. fm = 0.25[log{/3.7D+5.74/Re0.9}]-2, Re = VD/
Air 20C; = 1.2041 kg/m3, = 18.178E-6 Pas, sheet metal = 15E-5 mfm = 0.25[log{1/(24667D)+1/(3802.7(VD)0.9)}]-2 → fm(V,D)
Step 4. pL (pa/m) = fmV2/(2D) = fmV2/(1.661D) → pL(f,V,D)
Step 5. Find fb for each branch Qb by solve implicit eq.fb = 0.25[log{(pL/fbQb
2)0.2/24547+(fb/pL)0.18/(4747Qb
0.54)}]-2 → fb(f,Q,pL)
Step 6. Db = (fbQb2/(1.0246pL))
0.2 → Db(f,Q,pL)
Step 7. Vb = 4Qb/(Db2) → Vb(D,Q) check for appropriate, noise etc.
Step 2. Dmain (m) = (4Qmain/Vmain)0.5 → Dm(Q,V)
0.714
Step 8. Deq,f = 1.265(ab)0.6/(a+b)0.2 → D(a,b)
113 470700 0.0157 1.32 15.9
1.32
1.32
0.0161395500400.64 900.329.3
0.0182
19.8
17.21997000.42 40 370.147.1
35.7
41
Data: 1. pipe line diagram 2.Qmain & all Qbranch (cfm)
Duct Calculations by equations
Step 1. Select air velocity: Vmain (fpm) [cost, noise, install, maintenance]building; Vmain 800 – 2400 fpm, Vbrance 500 – 2000 fpm
Industrial; Vmain 2400 – 5000 fpm, Vbrance 2000 – 4000 fpm
Step 2. Dmain (in) = 12(4Qmain/Vmain)0.5 → Dm(Q,V)
Step 3. fm = 0.25[log{/3.7D+5.74/Re0.9}]-2, Re = VD/fm = 0.25[log{0.001596/D+0.86118/(VD)0.9}]-2 → fm(V,D)
Step 4. pL (in.wt/100 ft) =100fm(V/4009)2(12/D) =fm(V/401)212/D) →pL(f,V,D) Hw = (V/4009)2 = (V/60)2/(2gw/a) = V2 /(602*2*32.2/*(62.4/(12* 0.075))
Step 5. Find fb for each branch Qb by solve implicit eq.fb = 0.25[log{0.001328(pL/fbQb
2)0.2 +0.009334(fb/pLQb3)0.18}]-2 → fb(f,Q,pL)
Step 6. Db = 1.20255(fbQb2/pL)
0.2 → Db(f,Q,pL)
Step 7. Vb = 4Qb(12/Db)2/→ Vb(D,Q) check for appropriate, noise etc.
Step 8. Deq,f = 1.265(ab)0.6/(a+b)0.2 → D(a,b)
British unit:
D (in), V (fpm),
Q (cfm),
pL (in.wt/100 ft)
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Sample 18-8 (N.C. Harris, Modern Air Conditioning Practice). Size the simple duct system shown as below if the duct is for general office space and the maximum duct depth possible is 16 in. Each diffuser has a friction loss (pdiff) of 0.04 in.wg. Find the total static-pressure loss for the system.
Data: 1. PLD 2.Qmain & all Qbranch
3. hloss 0.04 in.wg. Of each diffuser
Find duct sizes and PL (in.wg.)
Step 1. Select Vmain = 2000 fpm (office) Step 2. Dmain (in) = 12(4Qmain/Vmain)0.5 → Dm(Q,V)
Step 3. fm = 0.25[log{0.001596/D+0.86118/(VD)0.9}]-2 → fm(V,D)
Step 4. pL (in.wt/100 ft) = fm(V/401)212/D) → pL(f,V,D)
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Sample 18-8 1. PLD 2.Qmain & all Qbranch 3. hloss 0.04 in.wg. Of each diffuser
Find duct sizes and PL (in.wg.)
Step 5. Find fb by solve implicit eq. F(fb) = 0F(fb) = fb - 0.25[log{0.001328(pL/fbQb
2)0.2 +0.009334(fb/pLQb3)0.18}]-2 = 0 → fb(f,Q,pL)
Step 6. Db = 1.20255(fbQb2/pL)
0.2 → Db(f,Q,pL)
Step 7. Vb = 4Qb(12/Db)2/ → Vb(D,Q)
Step 8. Deq,f = 1.265(ab)0.6/(a+b)0.2 → D(a,b)
total static-pressure loss = sum of equivalent lengthpL (in.wt/100 ft)
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Sample 18-8 1. PLD 2.Qmain & all Qbranch 3. hloss 0.04 in.wg. Of each diffuser
Find duct sizes and PL (in.wg.)
total static-pressure loss in ft = sum of duct length and equivalent length = Ltotal
total static-pressure loss in ft =pL (in.wt/100 ft)*Ltotal/100
Leq, diffuser = no of diffuser*pL (in.wt/100 ft)*100/pdiff
total static-pressure loss in ft = sum of Lduct + Leq
total static-pressure loss in ft =pL (in.wt/100 ft)*Ltotal/100
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Frictional Losses in Rectangular Ducts (Ch.18, N. C. Harris, Modern AC practice)
Rectangular Ducts: Aspect ratio < 8:1Dhydralic = 1.265(ab)3/5/(a+b)1/5 by laboratory studies
[But W.F. Stoecker R&A: Deq,f = 1.3(ab)0.625/(a+b)0.25]
V (fpm) & Hw (in. of water)v (fps) = (2gha)
0.5
ha = f (L/D)(V2/2g)ha = velocity pressure head, ftaha = wHw/12ha = 62.4Hw/(12a)ha = 5.2Hw/a
V/60 = (2g* 5.2Hw/a)0.5
g = 32.2 ft/s2, a = 0.075 lb/ft3
V = 4005Hw0.5
Supply air: Qs = qS /1.23(ts – ti)qS (W), t (C)
cfm = qS /1.08(ts – ti)qS (Btu/h), t (F)
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Prob:
Static-Pressure Losses in Duct Fitting
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Assume: low noise – specify V = 1300 fpm
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IJ:100 cfm
HI:700 cfm
GH:1300 cfm
FG:1900 cfm
AF:2200 cfm
1. Select V = 1300 fpm2. Given Qs = 3200 cfm at main duct and Qs or all duct sections3. Find ff = (Qs, V)
CD:200 cfmCE:200 cfm
BC:400 cfm
AB:1000 cfm
A:3200 cfm
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Use ff = 0.1 in. water per 100 ftin duct size calculation by equal-friction method
Fig. 18-15 Friction-loss chart for low-velocity straight ducts.
V = 1300 fpmQs = 3200 cfmff = 0.1 in. water per 100 ftof straight duct
Dh = 21.5 inA 3200 cfm, 22”, 1300 fpm
AF 2200 cfm, 18”, 1200 fpm
FG 1900 cfm, 17”, 1100 fpm
GH 1300 cfm, 15”, 1000 fpm
HI 700 cfm, 12” , 900 fpm
IJ 100 cfm, 12” , 550 fpm
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Fig. 18-16 Rectangular equivalents of round ducts.
Dh = 21.5 inAssume b = 12”Dh = 1.265(ab)3/5/(a+b)1/5
Main duct = 34” x 12”
AF 2200 cfm, 18”, 1200 fpm24” x 12”
FG 1900 cfm, 17”, 1100 fpm21” x 12”
GH 1300 cfm, 15”, 1000 fpm17” x 12”
HJ 700 cfm, 12” , 900 fpm12” x 12”
IJ 100 cfm, 12” , 550 fpm6” x 6”
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Duct Calculator- Imperial Unit Duct Calculator- SI Unit
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Duct Calculator- Imperial Unit
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Duct Calculator- SI Unit
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Duct CalculatorMain duct section A
V = 1300 fpmQs = 3200 cfmff = 0.115 in. water per 100 ft of straight duct
Round Dh = 21 in Assume b = 12”(ceiling space limit)Main duct A = 33” x 12”
Qs = 3200 cfm
ff = 0.115 in. wtper 100 ft
Dh = 21 in
Select b = 12”, a = 33“Rectangular duct a x b = 33” x 12”
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Duct CalculatorBranch duct section AF
ff = 0.115 in. wt /100 ftAF: Qs = 2200 cfmV = 1300 fpm
Round Dh = 18 in Assume b = 12”(ceiling space limit)duct AF = 24” x 12”
AF 2200 cfm
ff = 0.115 in. wt per 100 ft
DAF = 18 in
Select b = 12”, a = 24“Rectangular duct a x b = 24” x 12”
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Use ff = 0.1 in. water per 100 ft in duct size calculation by equal-friction method
3-4
1. Select V = 1300 fpm2. Given Qs = 3200 cfm at main duct and Qs or all duct sections3. Find ff = 0.1 in. water per 100 ft of straight duct4. Select ff = 0.1 in. w/100 ft5. Find Dh from (Qs, ff)6. Specify b, find a from Dh = 1.265(ab)3/5/(a+b)1/5
7. Check V = Q/(ab) gradually decrease ad duct size
5 612
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duct size calculation uing equal-friction method by calculations
12 3
45 67
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The total static pressure
ff = 0.028
L/W= 4
ff = 0.04
10% for friction loss by dampers included → htot = 0.283 in.wg
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Prob: Size SAD & RAD, fan static presureVSAD = 1500 fpmVRAD = 1300 fpm20% OAQsupply = 3800 cfm
Sizing Return-Air Ducts
Qreturn = 0.8*3800 = 3040 cfm = 800+1280+960
QOA = 0.2*3800 = 760 cfm
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12 3
45 67
3-45 6
12
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Min static pressure = SPsupply– (-SPreturn)
SPmin= 0.223– (-0.215) = 0.438 in.wg
SpsupplySpreturn
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Min static pressure = SPsupply– (-SPreturn)
SPmin= 0.219– (-0.261) = 0.480 in.wg
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The losses of coils, filters, and dampers must be added to determine the total fan static pressure.
Since the grille loss at J is only 0.05 in.wg, an excessive pressure difference exists across this return grille which will cause unwanted noise.A damper in stalled at J would have to be nearly closed to dissipate the static pressure and it would further increase the problem of noise.The best procedure is 1. to eliminate return-air locations close to fan or2. to minimize the return-duct losses by using larger duct. The latter choice adds to cost, of course.