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APPENDIX A
3-1-2010
Page A-9
NITROGEN CALCULATION PROCEDURE (Continued)
PIPING and FITTING NOTES: (Continued)
Table 6 – Pipe Pressure Loss (Nitrogen)
008528
STEP NO. 10 – DETERMINE ATOMIZER PRESSURE
LOSS
10a – Size Piping and Calculate Pipe Pressure Loss
(PPL) in Supply Line A:
Linear Length A1 through A4 + equivalent lengths of all
fittings in each pipe line x pressure loss (see Table 6) =
Pipe Pressure Loss (PPL).
Example:
1 in. Schedule 40 piping:
Length A1, 20 ft (6.096 m) + A2, 2 ft (0.610 m) + A3,
4.5 ft (1.372 m) + A4, 12 ft (3.658 m) + A5, 4 ft (1.219 m)
= 42.5 ft (12.957 m)
Equivalent length of 1-1/2 in. tee = 2.5 ft (0.76 m) (see
Table 1) Note: Because the full flow is going through one
branch of the tee treat it the same as an elbow of the
same size.
Equivalent length of 1 in. elbow = 2.5 ft (0.76 m) (see
Table 5)
Two elbows in Supply Line A = 2 x 2.5 ft (0.76 m) (equiva-
lent length per elbow) = 5.0 ft (1.52 m)
42.5 ft (12.957 m) + 2.5 ft (0.76 m)+ 5.0 ft (1.52 m) =
50.0 ft (15.33 m) total equivalent length of pipe
Select the correct pressure from (Table 8) for the number
of atomizers flowing through this pipe section. Since there
are four atomizers, the pressure loss factor would be
0.56339 psi/ft (0.12735 bar/m) (See Table 6).
You must also include the friction loss due to the 1 1/2 in
selector valve which has an equivalent length of 75.5 ft
(23.02 m) of 1 1/2 in pipe (See Table 5).
Select the correct pressure from (Table 8) for the number
of atomizers flowing through this selector valve. Since
there are four atomizers, the pressure loss factor would
be 0.06040 psi/ft (0.01365 bar/m) (See Table 6).
Pressure loss for Supply Line A = 50.0 ft (15.33 m) of
1 in. pipe x 0.56339 psi/ft (0.12735 bar/m) + 75.5 ft
(23.02 m) x 0.06040 psi/ft (0.01365 bar/m) = 32.73 psi
(2.266 bar).
Selector Valves
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
0.
12
79
8
0.
51
19
2
0.
03
52
1
0.
14
08
5
0.
31
69
1
0.
56
33
9
0.
03
41
9
0.
07
69
3
0.
13
67
7
0.
21
37
0
0.
30
77
3
0.
41
88
5
0.
54
70
7
0.
03
39
8
0.
06
04
0
0.
09
43
8
0.
13
59
0
0.
18
49
8
0.
24
16
1
0.
30
57
8
0.
37
75
1
0.
45
67
9
0.
54
36
2
0.
03
52
5
0.
04
79
8
0.
06
26
7
0.
07
93
2
0.
09
79
2
0.
11
84
9
0.
14
10
1
0.
16
54
9
0.
19
19
3
0.
22
03
3
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
0.
02
89
3
0.
11
57
2
0.
00
79
6
0.
03
18
4
0.
07
16
4
0.
12
73
5
0.
00
77
3
0.
01
73
9
0.
03
09
2
0.
04
83
1
0.
06
95
6
0.
09
46
8
0.
12
36
7
0.
00
76
8
0.
01
36
5
0.
02
13
3
0.
03
07
2
0.
04
18
1
0.
05
46
2
0.
06
91
2
0.
08
53
4
0.
10
32
6
0.
12
28
8
0.
00
79
7
0.
01
08
5
0.
01
41
7
0.
01
79
3
0.
02
21
4
0.
02
67
8
0.
03
18
8
0.
03
74
1
0.
04
33
9
0.
04
98
1
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2
Summary of Contents for ANSUL AQUASONIC
Page 84: ...SECTION V 3 1 2010 Page 5 14 NOTES Installation ...
Page 88: ...SECTION VII 3 1 2010 Page 7 2 Inspection NOTES ...
Page 94: ...SECTION VIII 3 1 2010 Page 8 6 NOTES Maintenance ...
Page 116: ...APPENDIX C 3 1 2010 Page C 2 Main and Reserve Systems NOTES ...
Page 134: ...APPENDIX D 3 1 2010 Page D 18 008567 Typical Examples ...
Page 135: ...APPENDIX D 3 1 2010 Page D 19 008568 Typical Examples ...
Page 136: ...APPENDIX D 3 1 2010 Page D 20 008569 Typical Examples ...
Page 137: ...APPENDIX D 3 1 2010 Page D 21 008570 Typical Examples ...
Page 138: ...APPENDIX D 3 1 2010 Page D 22 008571 Typical Examples ...
Page 139: ...APPENDIX D 3 1 2010 Page D 23 008572 Typical Examples ...
Page 140: ...APPENDIX D 3 1 2010 Page D 24 008573 Typical Examples ...
Page 141: ...APPENDIX D 3 1 2010 Page D 25 008574 Typical Examples ...