toilet exhaust riser.pdf
DESCRIPTION
Ventilation duct pressure loss calculation formatTRANSCRIPT
Item
No. Identification
Length
(m)
No of Fittings
& Accessories
Air Flow
Rate (L/S)
Duct
Velocity
(m/s)
Velocity
Pressure
(Pa)
Loss
Coefficients
for Fittings
Equivalent
Dia (mm)
Pressure
Drop
(Pa/m)
1.00 Straight Duct Section
1.01 a-b 1150 550 1.00 6,707 10.60 67.69 855.1 1.49
1.02 b-c 1150 550 1.00 6,707 10.60 67.69 855.1 1.49
1.03 c-d 1150 550 2.45 5,967 9.43 53.58 855.1 1.19
1.04 d-e 1000 550 2.45 5,967 10.85 70.86 801.8 1.65
1.05 e-f 1000 550 2.45 5,311 9.66 56.13 801.8 1.32
1.07 f-g 900 550 2.45 5,311 10.73 69.30 763.4 1.69
1.08 g-h 900 550 2.45 4,641 9.38 52.92 763.4 1.30
1.09 h-i 800 550 2.45 4,641 10.55 66.98 722.0 1.73
1.10 i-j 800 550 2.45 3,910 8.89 47.54 722.0 1.24
1.11 j-k 700 550 2.45 3,910 10.16 62.09 677.1 1.72
1.12 k-l 700 550 2.45 3,204 8.32 41.69 677.1 1.17
1.13 l-m 600 550 2.45 3,204 9.71 56.75 627.8 1.72
1.14 m-n 600 550 2.45 2,472 7.49 33.78 627.8 1.04
1.15 n-o 500 550 2.45 2,472 8.99 48.64 573.1 1.65
1.16 o-p 500 550 2.45 1,782 6.48 25.28 573.1 0.88
1.17 p-q 400 550 2.45 1,782 8.10 39.50 511.1 1.57
1.18 q-r 400 550 2.98 1,054 4.79 13.82 511.1 0.58
1.19 r-s 250 550 2.98 1,054 7.67 35.37 397.7 2.04
1.20 s-t 250 550 2.28 261 1.90 2.17 397.7 0.15
1.21 t-u 150 550 2.28 261 3.16 6.03 298.8 0.61
1.22 u-v 150 550 1.00 261 3.16 6.03 298.8 0.61
1.23 v-w 2.00 #DIV/0! #DIV/0! #DIV/0!
Duct Fittings
2.00 Bends & Elbows
2.01 b-Bend-90 Degree 1150 550 1 6,707 10.60 67.69 0.18 855.1
2.02 i-Bend-90 Degree 350 200 1 187 2.67 4.30 0.24 286.4
2.03 m-Bend-90 Degree 350 200 1 6,707 95.81 5526.59 0.19 286.4
2.04 w - Bend-90 Degree 850 450 1 2,825 7.39 32.84 0.19 667.7
Duct Size
2.05
ab,ac - Bend-90
Degree 494 552 2 2,825 10.36 64.61 0.21 570.6
3.00 Tees
3.01 c - Tee - main 200 200 1 25 0.63 0.24 2.23 218.6
3.02 d- Tee - Main 200 200 1 48 1.20 0.87 0.99 218.6
3.03 e- Tee - Main 200 200 1 73 1.83 2.01 0.57 218.6
3.04 f- Tee - Main 250 200 1 98 1.96 2.31 0.25 244.1
3.05 f1- Tee - Main 250 200 1 114 2.28 3.13 0.38 244.1
3.06 h- Tee - Main 250 200 1 172 3.44 7.12 0.10 244.1
3.07 j - Tee - main 350 200 1 187 2.67 4.30 0.10 286.4
3.08 k- Tee - main 350 200 1 210 3.00 5.42 0.10 286.4
3.09 l - Tee - main 350 200 1 235 3.36 6.78 0.10 286.4
3.10 n- Tee - main 400 300 1 260 2.17 2.83 2.53 377.7
3.11 o- Tee - main 600 350 1 545 2.60 4.05 0.99 496.5
3.12 p- Tee - main 600 350 1 830 3.95 9.40 0.61 496.5
3.13 q- Tee - main 700 400 1 1,115 3.98 9.55 0.38 572.9
3.14 r- Tee - main 700 400 1 1,400 5.00 15.05 0.30 572.9
3.15 s- Tee - main 850 450 1 1,685 4.41 11.68 0.25 667.7
3.16 t- Tee - main 850 450 1 1,685 4.41 11.68 0.18 667.7
3.17 u- Tee - main 850 450 1 2,255 5.90 20.92 0.10 667.7
3.18 v- Tee - main 850 450 1 2,540 6.64 26.55 0.10 667.7
3.19 g- Tee - branch 250 200 1 172 3.44 7.12 1.72 244.1
4.00 Transition
4.01
f- Transition (200x200 -
250x200) 200 200 1 98 2.45 3.61 0.14 218.6
4.02
i- Transition (250x200 -
350x200) 250 200 1 187 3.74 8.42 0.21 244.1
4.03
n- Transition (350x200
- 400x300) 350 200 1 260 3.71 8.31 0.29 286.4
4.04
o- Transition (400x300
- 600x350) 400 300 1 545 4.54 12.42 0.30 377.7
4.05
q- Transition (600x350-
700x400) 600 350 1 1,115 5.31 16.97 0.18 496.5
4.06
s- Transition (700x400-
850x450) 700 400 1 1,685 6.02 21.80 0.20 572.9
4.07
x- Transition (850x450-
900x915) 850 450 1 2,825 7.39 32.84 0.49 667.7
4.08
x- Transition (900x915-
494x552) 900 915 1 2,825 3.43 7.08 0.07 992.0
5.00 VCD
5.01 Airfoil blade 350 200 1 260 3.71 8.31 0.18 286.4 -
6.00 Flexible duct
6.01 150 1.00 1 25 1.41 0.70
7.00 Disk Valve
7.01 LVS/200/G1 - - 1 25 - - - -
8.00 Sound attenuator
8.01
MSA200-105-3-
PF/915x900x1500
9.00 Discharge louver
9.01 Bird guard mesh 494 552 1 2,825 10.36 64.61 0.58 570.6 -
External Static Pressure of Toilet Exhaust Fan (Pa)
Add 20% safety factor
Total External Static Pressure of Toilet Exhaust Fan (Pa)
Design Data from ASHRAE Unit
page 34.2 Velocity Pressure = 0.602 x V2
Time- s
Velocity - ms-1
Velocity = Flow Rate / Area Flow Rate - m3s
-1
Area - m2
Loss Coefficient
900
Bends r/w=1.0
Flexible duct pressure drop calculation
Re=66.4*V*Dh (eq 23, page 32.7)
f'=0.11 * ( Ɛ / Dh + 68 / Re) ^ 0.25
if f'>=0.018; f=f'
if f'< 0.018; f=0.85f'+0.0028
Duct diameter (Dh) 150 mm
Ɛ 3 mm
Re ###
f' 0.04
f 0.04
ΔPf 0.35 Pa/m
Correction factor 2
ΔPf 0.7 Pa/m
Total Pressure
Drop (Pa) Remarks
1.49
1.49
2.92
4.04
3.22
4.14
3.19
4.23
3.04
4.21
2.87
4.21
2.55
4.05
2.16
3.86
1.72
6.08
0.34
1.39
0.61
0.00
12.18 H/W=1, θ=90°, page 34.54, ASHRAE 2009 HB
1.05 H/W=0.57,K=1, r/W=1, Page21.52, ASHRAE 2009 HB 0.571429
1050.05 H/W=0.5,K=1, r/W=1, Page21.52, ASHRAE 2009 HB
6.24 H/W=1.9, K=1, r/W=1, Page 21.52,ASHRAE 2009 HB
27.14 H/W=1, K=1, r/W=1, Page 21.52,ASHRAE 2009 HB
0.52 Qs/Qc=0.52, Page 21.58, ASHRAE 2009 HB
0.86 Qs/Qc=0.66, Page 21.58, ASHRAE 2009 HB 0.657534
1.14 Qs/Qc=0.75, Page 21.58, ASHRAE 2009 HB 0.744898
0.58 Qs/Qc=0.86, Page 21.58, ASHRAE 2009 HB 0.859649
1.19 Qs/Qc=0.80, Page 21.58, ASHRAE 2009 HB
0.71 Qs/Qc=0.92, Page 21.58, ASHRAE 2009 HB 0.919786
0.43 Qs/Qc=0.89, Page 21.58, ASHRAE 2009 HB 0.890476
0.54 Qs/Qc=0.89, Page 21.58, ASHRAE 2009 HB 0.89
0.68 Qs/Qc=0.9, Page 21.58, ASHRAE 2009 HB 0.903846
7.16 Qs/Qc=0.48, Page 21.58, ASHRAE 2009 HB 0.477064
4.01 Qs/Qc=0.66, Page 21.58, ASHRAE 2009 HB 0.656627
5.72 Qs/Qc=0.74, Page 21.58, ASHRAE 2009 HB 0.744395
3.63 Qs/Qc=0.8, Page 21.58, ASHRAE 2009 HB 0.8
4.45 Qs/Qc=0.83, Page 21.58, ASHRAE 2009 HB 0.830861
2.94 Qs/Qc=0.86, Page 21.58, ASHRAE 2009 HB 0.85533
2.15 Qs/Qc=0.87, Page 21.58, ASHRAE 2009 HB 0.873614
2.09 Qs/Qc=0.89, Page 21.58, ASHRAE 2009 HB 0.887795
2.65 Qs/Qc=0.9, Page 21.58, ASHRAE 2009 HB 0.899115
12.25 Q1b/Qc=0.83, Table 14-13-I, SMACNA 1990
0.51 Refer ER4-1 page 21.58, ASHRAE 2009 HB
1.77 Refer ER4-1 page 21.58, ASHRAE 2009 HB
2.44 Refer ER4-1 page 21.58, ASHRAE 2009 HB
3.74 Refer ER4-1 page 21.58, ASHRAE 2009 HB
2.97 Refer ER4-1 page 21.58, ASHRAE 2009 HB
4.27 Refer ER4-1 page 21.58, ASHRAE 2009 HB
16.01 Refer ER4-1 page 21.58, ASHRAE 2009 HB
0.50 Refer Table 14-12-A page 14.27, SMACNA 1990
1.49 Refer CR9-4 page 21.57
0.70
calculated according to ASHRAE 1997 fundamentals, pg
32.7
10.00 Diagram 8, Type - LVS
39.00
37.47
n=0.7, A1/A0=1, Refer CR6-1 page 32.42, ASHRAE 2009
HB
1,333.05
266.61
1,599.66
1.66113 0.637105