PEXa Piping Systems Pressure Loss Tables

PEXa Piping Systems Pressure Loss Tables
REHAU PEXa PIPING SYSTEMS
PRESSURE LOSS TABLES
www.rehau.com
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TABLE OF CONTENTS
Scope. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .3
Pressure Loss Tables (supersede all previously published friction loss tables)
Table 1: With 100% Water. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 4
Table 2: With Water+20% Propylene Glycol. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 9
Table 3: With Water+50% Propylene Glycol. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 14
For updates to this publication and the most current REHAU technical guidelines, safety information and manufacturer’s recommendations,
visit na.rehau.com/resourcecenter
2
855.681 en 03.2015
SCOPE
This technical information applies to the planning, installation
and connection of REHAU sustainable products using REHAU's
extensive range of PEXa pipes.
The designer should also review the pertinent REHAU technical
instructions and the REHAU PEXa Limited Warranty before beginning
to design a system with PEXa pipes.
Pressure loss tables are typically used when manually designing PEXa
piping systems for hydronic applications including radiant heating/
cooling, snow and ice melting, soil conditioning, geothermal ground
loops, PEX plumbing and water service, energy transfer and outdoor
wood boiler. These tables are used to properly size the circulator for
the PEXa pipes. The designer must ensure the flow requirement and
pressure loss are within the circulator's performance capability. Use
the REHAU LoopCAD® Software which includes a built-in calculator for
pipe pressure losses for additional data not found in these tables.
After reading the appropriate REHAU Design Guide, designers should
attend the Skill Builders Complete seminar offered by the REHAU
Academy, where design techniques are more fully explored. Designers should also periodically check the REHAU Resource Center for the
latest updates to the technical instructions.
855.681 en 03.2015
If you do not have prior experience with hydronic heating systems or
require additional assistance, please contact your regional REHAU
sales office.
3
Table
1A:Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
Pipe Water
With 100% Water
Table 1A:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 100%
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) Water
120°F (49°C) Water
180°F (82°C) Water
GPM
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
0.1
0.3
0.2
0.1
0.1
0.18
0.06
0.03
0.01
0.09
0.03
0.01
<.01
0.10
0.02
<.01
<.01
0.2
0.6
0.3
0.2
0.2
0.36
0.11
0.05
0.03
0.39
0.10
0.03
0.01
0.33
0.08
0.03
0.02
0.3
0.9
0.5
0.4
0.3
0.98
0.17
0.08
0.04
0.78
0.19
0.08
0.04
0.67
0.16
0.07
0.03
0.4
1.3
0.7
0.5
0.4
1.58
0.39
0.11
0.06
1.28
0.31
0.13
0.06
1.11
0.27
0.11
0.05
0.5
1.6
0.9
0.6
0.4
2.30
0.57
0.24
0.07
1.88
0.46
0.19
0.09
1.64
0.39
0.16
0.08
0.6
1.9
1.0
0.7
0.5
3.14
0.77
0.32
0.16
2.58
0.62
0.26
0.13
2.27
0.54
0.22
0.11
0.7
2.2
1.2
0.8
0.6
4.09
1.00
0.42
0.20
3.38
0.81
0.34
0.16
2.99
0.71
0.29
0.14
0.8
2.5
1.4
1.0
0.7
5.15
1.26
0.52
0.25
4.28
1.03
0.42
0.21
3.79
0.90
0.37
0.18
0.9
2.8
1.6
1.1
0.8
6.31
1.54
0.64
0.31
5.27
1.26
0.52
0.25
4.69
1.11
0.45
0.22
1.0
3.2
1.7
1.2
0.9
7.58
1.84
0.77
0.37
6.35
1.52
0.63
0.30
5.67
1.34
0.55
0.26
1.2
3.8
2.1
1.4
1.1
10.4
2.52
1.04
0.51
8.80
2.09
0.86
0.41
7.89
1.85
0.76
0.36
1.4
4.4
2.4
1.7
1.2
13.6
3.29
1.36
0.66
11.6
2.75
1.13
0.54
10.5
2.44
0.99
0.47
1.6
5.0
2.8
1.9
1.4
17.3
4.15
1.71
0.83
14.8
3.48
1.42
0.68
13.4
3.11
1.26
0.60
1.8
5.7
3.1
2.2
1.6
21.3
5.09
2.10
1.01
18.3
4.29
1.75
0.84
16.6
3.84
1.56
0.74
2.0
6.3
3.5
2.4
1.8
25.7
6.13
2.52
1.22
22.1
5.18
2.12
1.01
20.2
4.65
1.88
0.90
2.2
6.9
3.8
2.6
1.9
30.4
7.24
2.98
1.43
26.4
6.15
2.51
1.20
24.1
5.54
2.24
1.06
2.4
7.6
4.2
2.9
2.1
35.5
8.44
3.47
1.67
30.9
7.20
2.93
1.40
28.3
6.49
2.62
1.24
2.6
8.2
4.5
3.1
2.3
41.0
9.72
3.99
1.92
35.8
8.32
3.38
1.61
32.9
7.52
3.03
1.43
2.8
8.8
4.9
3.4
2.5
46.9
11.1
4.55
2.18
41.1
9.51
3.86
1.84
37.8
8.62
3.47
1.64
3.0
9.5
53.1
46.6
43.1
9.79
3.93
1.86
11.0
4.42
2.09
3.2
5.2
3.6
2.6
5.6
3.8
2.8
12.5
5.13
2.46
14.1
5.75
2.76
10.8
4.37
2.08
12.1
4.90
2.33
3.4
5.9
4.1
3.0
15.7
6.40
3.07
13.5
5.47
2.60
12.3
4.94
2.33
3.6
6.3
4.3
3.2
17.3
7.09
3.39
15.0
6.07
2.88
13.7
5.49
2.59
3.8
6.6
4.6
3.3
19.1
7.80
3.73
16.6
6.69
3.17
15.2
6.06
2.85
4.0
6.9
4.8
3.5
20.9
8.54
4.08
18.2
7.34
3.48
16.7
6.66
3.13
4.2
7.3
5.0
3.7
22.9
9.31
4.45
19.9
8.02
3.80
18.3
7.29
3.43
4.4
7.6
5.3
3.9
24.8
10.1
4.83
21.7
8.73
4.13
19.9
7.94
3.73
4.6
8.0
5.5
4.1
26.9
11.0
5.23
23.6
9.47
4.48
21.7
8.63
4.05
4.8
8.3
5.7
4.2
29.1
11.8
5.64
25.5
10.2
4.84
23.5
9.33
4.38
5.0
8.7
6.0
4.4
31.3
12.7
6.06
27.5
11.0
5.21
25.3
10.1
4.72
5.5
9.6
6.6
4.8
37.2
15.1
7.18
32.8
13.1
6.19
30.3
12.0
5.62
6.0
7.2
5.3
17.6
8.39
15.4
7.25
14.1
6.61
6.5
7.8
5.7
20.4
9.68
17.9
8.40
16.4
7.66
7.0
8.4
6.2
23.3
11.1
20.5
9.62
18.9
8.80
7.5
9.0
6.6
26.4
12.5
23.3
10.9
21.5
10.0
8.0
9.6
7.0
29.7
14.0
26.2
12.3
24.3
8.5
7.5
15.7
13.7
11.3
12.6
9.0
7.9
17.4
15.3
14.1
9.5
8.4
19.2
16.9
15.6
10.0
8.8
21.0
18.6
17.1
11.0
9.7
25.0
22.2
20.5
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
values loss,
shown
in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
4
lee 2163, Page 1 / 15
855.681 en 03.2015
Table
1B:Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
Pipe Water
With 100% Water
Table 1B:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 100%
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) Water
120°F (49°C) Water
180°F (82°C) Water
GPM
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1
0.5
0.4
0.3
0.1
0.11
0.04
0.01
<.01
0.09
0.04
0.02
<.01
0.08
0.03
0.01
<.01
2
1.1
0.7
0.5
0.3
0.37
0.14
0.07
0.02
0.31
0.12
0.05
0.01
0.27
0.10
0.05
0.01
3
1.6
1.1
0.8
0.4
0.75
0.29
0.13
0.04
0.62
0.24
0.11
0.03
0.55
0.21
0.09
0.03
4
2.1
1.4
1.0
0.6
1.23
0.48
0.22
0.06
1.04
0.40
0.18
0.05
0.92
0.35
0.16
0.04
5
2.7
1.8
1.3
0.7
1.82
0.70
0.32
0.09
1.54
0.59
0.26
0.07
1.39
0.52
0.23
0.06
6
3.2
2.1
1.5
0.9
2.51
0.96
0.44
0.12
2.14
0.82
0.37
0.10
1.93
0.73
0.33
0.09
7
3.7
2.5
1.8
1.0
3.30
1.27
0.57
0.16
2.83
1.07
0.48
0.13
2.56
0.96
0.43
0.12
8
4.3
2.9
2.0
1.2
4.19
1.60
0.72
0.20
3.61
1.37
0.61
0.17
3.27
1.23
0.55
0.15
9
4.8
3.2
2.3
1.3
5.17
1.97
0.89
0.25
4.47
1.69
0.75
0.21
4.07
1.52
0.68
0.18
10
5.3
3.6
2.6
1.5
6.24
2.38
1.07
0.30
5.42
2.04
0.91
0.25
4.94
1.85
0.82
0.22
11
5.9
3.9
2.8
1.6
7.40
2.82
1.27
0.35
6.45
2.43
1.08
0.30
5.90
2.20
0.97
0.26
12
6.4
4.3
3.1
1.8
8.66
3.29
1.48
0.41
7.57
2.84
1.27
0.35
6.94
2.58
1.14
0.31
13
6.9
4.6
3.3
1.9
10.0
3.80
1.70
0.47
8.77
3.29
1.46
0.40
8.06
3.00
1.32
0.36
14
7.5
5.0
3.6
2.1
11.4
4.34
1.94
0.53
10.1
3.77
1.67
0.46
9.26
3.44
1.51
0.41
15
8.0
5.4
3.8
2.2
13.0
4.91
2.20
0.60
11.4
4.27
1.90
0.52
10.5
3.91
1.72
0.46
16
8.5
5.7
4.1
2.4
14.6
5.51
2.47
0.68
12.9
4.81
2.13
0.58
11.9
4.40
1.94
0.52
17
9.1
6.1
4.4
2.5
16.3
6.15
2.75
0.75
14.4
5.38
2.38
0.65
13.3
4.93
2.17
0.58
18
9.6
18.0
16.0
14.9
19
6.4
4.6
2.7
6.8
4.9
2.8
6.82
3.04
0.83
7.52
3.35
0.92
5.97
2.64
0.72
6.60
2.92
0.79
5.48
2.41
0.65
6.07
2.66
0.71
20
7.1
5.1
3.0
8.25
3.68
1.01
7.26
3.20
0.87
6.68
2.93
0.78
22
7.9
5.6
3.3
9.80
4.37
1.19
8.65
3.82
1.03
7.99
3.49
0.93
24
8.6
6.1
3.6
11.5
5.11
1.39
10.2
4.48
1.20
9.41
4.11
1.09
26
9.3
6.7
3.9
13.3
5.91
1.61
11.8
5.19
1.39
10.9
4.77
1.27
1.45
28
7.2
4.2
6.75
1.84
5.95
1.60
5.48
30
7.7
4.5
7.66
2.08
6.76
1.81
6.24
1.65
32
8.2
4.8
8.61
2.34
7.62
2.04
7.05
1.86
34
8.7
5.1
9.62
2.61
8.53
2.28
7.90
2.08
36
9.2
5.4
10.7
2.89
9.49
2.53
8.80
2.32
38
9.7
5.7
11.8
3.19
10.5
2.79
9.75
40
6.0
3.49
3.07
2.56
2.82
42
6.3
3.82
3.36
3.09
44
6.6
4.15
3.66
3.37
46
6.9
4.50
3.97
3.66
48
7.2
4.87
4.30
3.97
50
7.5
5.24
4.64
4.28
52
7.8
5.63
4.99
4.61
54
8.1
6.03
5.35
4.95
56
8.4
6.44
5.72
5.30
58
8.7
6.87
6.11
5.66
60
9.0
7.31
6.51
6.04
65
9.7
8.46
7.56
7.03
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressure
terms
of noise or erosion of the system components.
– Flow velocity
8and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
valuesloss,
shown
in pressure loss units of psi per 100 ft (30.5 m) of
pipe.
noise or
multiply the value
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 2 / 15
5
Table
1C: Pressure
Pressure
Loss
Metric-Sized
PEXaPipe
Carrier
PipeWater
With 100% Water
Table 1C:
Loss
for for
Metric-Sized
SDR11SDR11
REHAU REHAU
PEXa Carrier
with 100%
pressure loss in psi per 100 ft of pipe
Flow
ft/sec
Rate
60°F (16°C) Water
120°F (49°C) Water
180°F (82°C) Water
GPM
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
0.1
0.4
0.1
<0.1
<0.1
0.29
<.01
<.01
<.01
0.14
<.01
<.01
<.01
0.18
<.01
<.01
<.01
0.2
0.8
0.1
0.1
<0.1
0.58
0.01
<.01
<.01
0.67
<.01
<.01
<.01
0.58
<.01
<.01
<.01
0.3
1.2
0.2
0.1
0.1
1.67
0.02
<.01
<.01
1.34
0.01
<.01
<.01
1.16
0.01
<.01
<.01
0.4
1.6
0.2
0.2
0.1
2.71
0.03
0.01
<.01
2.21
0.03
<.01
<.01
1.93
0.02
<.01
<.01
0.5
2.0
0.3
0.2
0.1
3.97
0.04
0.01
<.01
3.25
0.04
0.01
<.01
2.86
0.03
0.01
<.01
0.6
2.4
0.4
0.2
0.1
5.42
0.04
0.02
<.01
4.48
0.06
0.02
<.01
3.96
0.05
0.01
<.01
0.7
2.8
0.4
0.3
0.2
7.07
0.09
0.02
<.01
5.88
0.07
0.02
<.01
5.22
0.06
0.02
<.01
0.8
3.2
0.5
0.3
0.2
8.90
0.11
0.02
<.01
7.45
0.09
0.03
0.01
6.64
0.08
0.02
<.01
0.9
3.6
0.6
0.3
0.2
10.9
0.14
0.04
<.01
9.18
0.11
0.03
0.01
8.22
0.10
0.03
0.01
1.0
4.0
0.6
0.4
0.2
13.1
0.17
0.05
0.01
11.1
0.13
0.04
0.01
9.95
0.12
0.04
0.01
1.2
4.8
0.7
0.5
0.3
18.1
0.22
0.07
0.03
15.4
0.18
0.06
0.02
13.9
0.16
0.05
0.02
1.4
5.6
0.9
0.5
0.3
23.7
0.29
0.09
0.03
20.3
0.24
0.07
0.03
18.4
0.21
0.06
0.02
1.6
6.3
1.0
0.6
0.4
30.1
0.37
0.11
0.04
25.9
0.30
0.09
0.03
23.6
0.26
0.08
0.03
1.8
7.1
1.1
0.7
0.4
37.1
0.45
0.14
0.05
32.1
0.37
0.11
0.04
29.4
0.32
0.10
0.03
2.0
7.9
1.2
0.8
0.5
44.8
0.54
0.17
0.06
39.0
0.44
0.14
0.05
35.8
0.39
0.12
0.04
2.2
8.7
1.4
0.8
0.5
53.1
0.63
0.20
0.07
46.5
0.52
0.16
0.06
42.8
0.46
0.14
0.05
2.4
9.5
1.5
0.9
0.6
62.1
0.74
0.23
0.08
54.6
0.61
0.19
0.07
50.4
0.54
0.16
0.06
2.6
1.6
1.0
0.6
0.85
0.26
0.09
0.70
0.21
0.08
0.62
0.19
0.07
2.8
1.7
1.1
0.7
0.96
0.30
0.11
0.80
0.24
0.09
0.71
0.22
0.08
3.0
1.9
1.1
0.7
1.08
0.33
0.12
0.91
0.28
0.10
0.81
0.24
0.09
4.0
2.5
1.5
1.0
1.79
0.55
0.19
1.51
0.46
0.16
1.35
0.41
0.14
5.0
3.1
1.9
1.2
2.65
0.81
0.29
2.26
0.68
0.24
2.03
0.61
0.21
6.0
3.7
2.3
1.5
3.66
1.11
0.39
3.13
0.94
0.33
2.83
0.84
0.29
0.39
7.0
4.4
2.7
1.7
4.81
1.46
0.51
4.14
1.24
0.43
3.76
1.11
8.0
5.0
3.0
2.0
6.11
1.85
0.65
5.28
1.58
0.55
4.81
1.42
0.49
10.0
6.2
3.8
2.4
9.11
2.75
0.96
7.95
2.36
0.82
7.28
2.14
0.73
12.0
7.5
4.6
2.9
12.7
3.80
1.33
11.1
3.29
1.14
10.2
2.99
1.02
14.0
8.7
5.3
3.4
16.7
5.01
1.75
14.8
4.36
1.50
13.7
3.98
1.36
16.0
6.1
3.9
6.38
2.22
5.57
1.91
5.11
1.74
18.0
6.8
4.4
7.89
2.74
6.92
2.37
6.36
2.16
20.0
7.6
4.9
9.54
3.30
8.41
2.88
7.75
2.62
22.0
8.4
5.4
11.3
3.92
10.0
3.42
9.27
3.13
24.0
9.1
5.9
13.3
4.59
11.8
4.02
10.9
3.68
26.0
9.9
6.4
15.4
5.30
13.7
4.66
12.7
4.28
28.0
6.9
6.06
5.34
4.91
30.0
7.3
6.87
6.06
5.59
32.0
7.8
7.73
6.83
6.31
34.0
8.3
8.63
7.65
7.08
36.0
8.8
9.58
8.51
7.88
38.0
9.3
10.6
9.41
8.73
40.0
9.8
11.6
10.4
9.62
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
values loss,
shown
in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
6
lee 2163, Page 3 / 15
855.681 en 03.2015
Table
1D:Pressure
Pressure
Loss
Metric-Sized
PEXaPipe
Carrier
PipeWater
With 100% Water
Table 1D:
Loss
for for
Metric-Sized
SDR11SDR11
REHAU REHAU
PEXa Carrier
with 100%
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) Water
120°F (49°C) Water
180°F (82°C) Water
GPM
50
63
75
90
50
63
75
90
50
63
75
90
50
63
75
90
2
0.3
0.2
0.1
0.1
0.02
<.01
<.01
<.01
0.02
<.01
<.01
<.01
0.01
<.01
<.01
<.01
4
0.6
0.4
0.3
0.2
0.07
0.02
<.01
<.01
0.06
0.02
<.01
<.01
0.05
0.02
<.01
<.01
6
0.9
0.6
0.4
0.3
0.14
0.05
0.02
<.01
0.11
0.04
0.02
<.01
0.10
0.03
0.01
<.01
8
1.3
0.8
0.6
0.4
0.22
0.07
0.03
0.01
0.19
0.06
0.03
0.01
0.17
0.05
0.02
<.01
10
1.6
1.0
0.7
0.5
0.33
0.11
0.05
0.02
0.28
0.09
0.04
0.02
0.25
0.08
0.03
0.01
12
1.9
1.2
0.8
0.6
0.45
0.15
0.06
0.03
0.38
0.13
0.05
0.02
0.34
0.11
0.05
0.02
14
2.2
1.4
1.0
0.7
0.60
0.20
0.09
0.04
0.51
0.17
0.07
0.03
0.46
0.15
0.06
0.03
16
2.5
1.6
1.1
0.8
0.75
0.25
0.11
0.05
0.65
0.21
0.09
0.04
0.58
0.19
0.08
0.03
18
2.8
1.8
1.2
0.9
0.93
0.31
0.13
0.06
0.80
0.26
0.11
0.05
0.72
0.23
0.10
0.04
20
3.1
2.0
1.4
1.0
1.12
0.37
0.16
0.07
0.97
0.32
0.13
0.06
0.87
0.28
0.12
0.05
22
3.4
2.2
1.5
1.1
1.33
0.44
0.19
0.08
1.15
0.38
0.16
0.07
1.04
0.34
0.14
0.06
24
3.8
2.4
1.7
1.2
1.55
0.51
0.22
0.09
1.34
0.44
0.19
0.08
1.22
0.40
0.17
0.07
26
4.1
2.6
1.8
1.2
1.79
0.59
0.25
0.11
1.56
0.51
0.22
0.09
1.42
0.46
0.19
0.08
28
4.4
2.8
1.9
1.3
2.05
0.68
0.29
0.12
1.78
0.58
0.25
0.10
1.62
0.52
0.22
0.09
30
4.7
3.0
2.1
1.4
2.32
0.76
0.33
0.14
2.02
0.66
0.28
0.12
1.84
0.60
0.25
0.10
35
5.5
3.5
2.4
1.7
3.06
1.01
0.43
0.18
2.68
0.87
0.37
0.15
2.46
0.79
0.33
0.14
40
6.3
3.9
2.8
1.9
3.90
1.28
0.54
0.23
3.43
1.11
0.47
0.19
3.15
1.01
0.42
0.18
45
7.0
4.4
3.1
2.2
4.83
1.58
0.67
0.28
4.26
1.38
0.58
0.24
3.93
1.26
0.53
0.22
50
7.8
4.9
3.5
2.4
5.85
1.91
0.81
0.34
5.18
1.67
0.70
0.29
4.79
1.53
0.64
0.26
55
8.6
5.4
3.8
2.6
6.96
2.27
0.96
0.40
6.19
1.99
0.84
0.35
5.73
1.83
0.76
0.31
60
9.4
5.9
4.1
2.9
8.16
2.66
1.13
0.47
7.28
2.34
0.98
0.41
6.76
2.15
0.90
0.37
65
6.4
4.5
3.1
3.07
1.30
0.54
2.71
1.14
0.47
2.50
1.04
0.43
70
6.9
4.8
3.4
3.52
1.49
0.62
3.11
1.30
0.54
2.87
1.19
0.49
75
7.4
5.2
3.6
3.99
1.68
0.70
3.53
1.48
0.61
3.27
1.36
0.56
80
7.9
5.5
3.8
4.49
1.89
0.79
3.99
1.67
0.69
3.69
1.53
0.63
85
8.4
5.9
4.1
5.01
2.11
0.88
4.46
1.86
0.77
4.14
1.71
0.70
90
8.9
6.2
4.3
5.57
2.35
0.97
4.96
2.07
0.85
4.61
1.91
0.78
95
9.4
6.6
4.6
6.15
2.59
1.07
5.49
2.29
0.94
5.10
2.11
0.86
100
9.9
6.9
4.8
6.75
2.84
1.18
6.04
2.52
1.03
5.62
2.32
0.95
105
7.3
5.0
3.11
1.29
2.76
1.13
2.55
1.04
110
7.6
5.3
3.38
1.40
3.00
1.23
2.78
1.13
115
7.9
5.5
3.67
1.52
3.26
1.34
3.02
1.23
120
8.3
5.8
3.97
1.64
3.53
1.45
3.28
1.33
130
9.0
6.2
4.59
1.90
4.10
1.68
3.81
1.55
140
9.7
6.7
5.26
2.17
4.71
1.93
4.39
1.78
150
7.2
2.46
2.19
2.02
160
7.7
2.77
2.47
2.29
170
8.2
3.10
2.76
2.56
180
8.7
3.44
3.07
2.86
190
9.1
3.80
3.40
3.16
200
9.6
4.18
3.74
3.49
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
considered excessive and
psi per 100 ft
terms of
may result in excessive
of pipe.
feet of head,
pressure loss, noise or
multiply the value
erosion of above
system 8 fps (2.5 m/s) might
Example:
for 200
by 2.307.
– Flow velocity
result
in excessive pressurelisted
loss,
noise or erosion of the system components.
components.
lineal ft of pipe,
– Table values shown in pressure loss units
of
psi
per
100
ft
(30.5
m)
of
pipe.
double the value
Example: 1 psi =
listed the
in this
table. listed in this table.2.307 ft of head
Example: for 200 lineal ft of pipe, double
value
– To express pressure loss in terms of feet of head, multiply the table value by 2.307.
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 4 / 15
7
Table
1E: Pressure Loss for Metric-Sized SDR11 REHAU PEXa Carrier Pipe With 100% Water
Table 1E
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) Water
120°F (49°C) Water
180°F (82°C) Water
GPM
110
125
140
160
110
125
140
160
110
125
140
160
110
125
140
160
5
0.2
0.1
0.1
0.1
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
10
0.3
0.2
0.2
0.2
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
15
0.5
0.4
0.3
0.2
0.02
<.01
<.01
<.01
0.01
<.01
<.01
<.01
0.01
<.01
<.01
<.01
20
0.6
0.5
0.4
0.3
0.03
0.01
<.01
<.01
0.02
0.01
<.01
<.01
0.02
0.01
<.01
<.01
25
0.8
0.6
0.5
0.4
0.04
0.02
0.01
<.01
0.03
0.02
0.01
<.01
0.03
0.02
<.01
<.01
30
1.0
0.7
0.6
0.5
0.05
0.03
0.02
<.01
0.04
0.02
0.01
<.01
0.04
0.02
0.01
<.01
40
1.3
1.0
0.8
0.6
0.09
0.05
0.03
0.01
0.07
0.04
0.02
0.01
0.07
0.04
0.02
0.01
50
1.6
1.2
1.0
0.8
0.13
0.07
0.04
0.02
0.11
0.06
0.03
0.02
0.10
0.05
0.03
0.02
60
1.9
1.5
1.2
0.9
0.18
0.10
0.06
0.03
0.15
0.08
0.05
0.03
0.14
0.07
0.04
0.02
70
2.3
1.7
1.4
1.1
0.24
0.13
0.07
0.04
0.20
0.11
0.06
0.03
0.18
0.10
0.06
0.03
80
2.6
2.0
1.6
1.2
0.30
0.16
0.09
0.05
0.26
0.14
0.08
0.04
0.23
0.13
0.07
0.04
90
2.9
2.2
1.8
1.4
0.37
0.20
0.12
0.06
0.32
0.17
0.10
0.05
0.29
0.16
0.09
0.05
100
3.2
2.5
2.0
1.5
0.45
0.24
0.14
0.07
0.39
0.21
0.12
0.06
0.35
0.19
0.11
0.06
110
3.5
2.7
2.2
1.7
0.53
0.29
0.17
0.09
0.46
0.25
0.14
0.08
0.42
0.23
0.13
0.07
120
3.9
3.0
2.4
1.8
0.62
0.34
0.19
0.10
0.54
0.29
0.17
0.09
0.50
0.27
0.15
0.08
0.09
130
4.2
3.2
2.6
2.0
0.72
0.39
0.22
0.12
0.63
0.34
0.19
0.10
0.58
0.31
0.18
140
4.5
3.5
2.8
2.1
0.82
0.44
0.26
0.14
0.72
0.39
0.22
0.12
0.66
0.35
0.20
0.11
150
4.8
3.7
3.0
2.3
0.93
0.50
0.29
0.15
0.82
0.44
0.25
0.13
0.75
0.40
0.23
0.12
160
5.1
4.0
3.2
2.4
1.05
0.56
0.33
0.17
0.92
0.50
0.28
0.15
0.85
0.45
0.26
0.14
170
5.5
4.2
3.4
2.6
1.17
0.63
0.36
0.19
1.03
0.55
0.32
0.17
0.95
0.51
0.29
0.15
180
5.8
4.5
3.6
2.7
1.30
0.70
0.40
0.21
1.15
0.61
0.35
0.19
1.06
0.56
0.32
0.17
190
6.1
4.7
3.8
2.9
1.43
0.77
0.44
0.23
1.27
0.68
0.39
0.20
1.17
0.62
0.36
0.19
200
6.4
5.0
4.0
3.0
1.57
0.85
0.49
0.26
1.39
0.75
0.43
0.22
1.29
0.69
0.39
0.20
225
7.2
5.6
4.5
3.4
1.95
1.05
0.60
0.32
1.74
0.93
0.53
0.28
1.61
0.85
0.49
0.25
250
8.0
6.2
5.0
3.8
2.36
1.27
0.73
0.39
2.11
1.13
0.64
0.34
1.96
1.04
0.59
0.31
275
8.8
6.9
5.5
4.2
2.82
1.51
0.87
0.46
2.52
1.35
0.77
0.40
2.35
1.25
0.71
0.37
300
9.7
3.31
2.97
2.77
325
7.5
6.0
4.6
8.1
6.4
4.9
1.78
1.02
0.54
2.06
1.18
0.62
1.58
0.90
0.47
1.84
1.05
0.55
1.47
0.83
0.43
1.71
0.97
0.50
350
8.7
6.9
5.3
2.36
1.35
0.71
2.11
1.20
0.63
1.96
1.11
0.58
375
9.4
7.4
5.7
2.68
1.53
0.81
2.40
1.37
0.71
2.24
1.27
0.66
400
10.0
7.9
6.1
3.02
1.73
0.91
2.71
2.53
8.4
6.5
1.93
1.01
425
1.54
0.81
1.73
0.90
1.43
0.74
1.61
0.83
450
8.9
6.9
2.14
1.13
1.92
1.00
1.79
0.93
475
9.4
7.2
2.37
1.24
2.13
1.11
1.98
1.03
500
9.9
7.6
2.60
1.37
2.34
1.22
2.19
525
8.0
1.49
1.34
1.13
1.24
550
8.4
1.63
1.46
1.36
575
8.8
1.77
1.59
1.48
600
9.1
1.91
1.72
1.60
625
9.5
2.06
1.85
1.73
650
9.9
2.21
2.00
1.86
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
considered excessive and
psi per 100 ft
terms of
may result in excessive
of pipe.
feet of head,
value
– Flow velocity above 8 fps (2.5 m/s) might result in excessive pressuremultiply
loss, the
noise
or erosion of the system components.
erosion of system
Example: for 200
listed by 2.307.
– Table values
shown in pressure loss units
components.
lineal ftof
of psi
pipe,per 100 ft (30.5 m) of pipe.
double the value
Example: for 200 lineal ft of pipe, double
the value listed in this table.Example: 1 psi =
listed in this table.
2.307 ft of head
– To express pressure loss in terms of feet of head, multiply the table value by 2.307.
Example: 1 psi = 2.307 ft of head.
pressure loss, noise or
2.20150309-pressureloss_raupex_rautherm(emailcopyonly) (1).xlsx
8
lee 2163, Page 1 / 1
855.681 en 03.2015
Table
2A:Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
PipeWater
With/ 20%
80%Propylene
Water / 20%
Table 2A:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 80%
GlycolPropylene Glycol
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 20% Glycol
120°F (49°C) 20% Glycol
180°F (82°C) 20% Glycol
GPM
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
0.1
0.3
0.2
0.1
0.1
0.38
0.11
0.05
0.03
0.16
0.05
0.02
0.01
0.09
0.03
0.01
<.01
0.2
0.6
0.3
0.2
0.2
0.75
0.23
0.11
0.06
0.32
0.10
0.05
0.02
0.39
0.10
0.03
0.01
0.3
0.9
0.5
0.4
0.3
1.13
0.34
0.16
0.09
0.94
0.14
0.07
0.04
0.77
0.19
0.08
0.04
0.4
1.3
0.7
0.5
0.4
1.51
0.46
0.22
0.12
1.52
0.37
0.09
0.05
1.26
0.31
0.13
0.06
0.5
1.6
0.9
0.6
0.4
1.88
0.57
0.27
0.15
2.22
0.55
0.23
0.11
1.86
0.45
0.19
0.09
0.6
1.9
1.0
0.7
0.5
4.01
0.69
0.33
0.18
3.03
0.74
0.31
0.15
2.56
0.62
0.26
0.12
0.7
2.2
1.2
0.8
0.6
5.18
0.80
0.38
0.21
3.95
0.96
0.40
0.20
3.35
0.81
0.33
0.16
0.8
2.5
1.4
1.0
0.7
6.49
0.92
0.44
0.24
4.98
1.21
0.50
0.24
4.24
1.02
0.42
0.20
0.9
2.8
1.6
1.1
0.8
7.91
1.95
0.49
0.26
6.11
1.48
0.62
0.30
5.22
1.25
0.52
0.25
1.0
3.2
1.7
1.2
0.9
9.46
2.33
0.98
0.29
7.35
1.78
0.74
0.36
6.30
1.50
0.62
0.30
1.2
3.8
2.1
1.4
1.1
12.9
3.17
1.33
0.65
10.1
2.44
1.01
0.49
8.73
2.07
0.85
0.41
1.4
4.4
2.4
1.7
1.2
16.8
4.11
1.72
0.84
13.3
3.19
1.32
0.64
11.5
2.72
1.12
0.54
1.6
5.0
2.8
1.9
1.4
21.1
5.16
2.15
1.05
16.8
4.02
1.66
0.80
14.7
3.45
1.41
0.68
1.8
5.7
3.1
2.2
1.6
25.9
6.31
2.63
1.27
20.7
4.95
2.04
0.98
18.1
4.26
1.74
0.83
2.0
6.3
3.5
2.4
1.8
31.1
7.55
3.14
1.52
25.0
5.95
2.45
1.18
22.0
5.14
2.10
1.00
2.2
6.9
3.8
2.6
1.9
36.7
8.90
3.70
1.79
29.7
7.04
2.89
1.39
26.2
6.11
2.49
1.19
2.4
7.6
4.2
2.9
2.1
42.7
10.3
4.29
2.08
34.7
8.22
3.37
1.62
30.7
7.14
2.90
1.38
2.6
8.2
4.5
3.1
2.3
49.2
11.9
4.92
2.38
40.1
9.47
3.88
1.86
35.6
8.25
3.35
1.60
2.8
8.8
4.9
3.4
2.5
56.0
13.5
5.59
2.70
45.9
10.8
4.42
2.12
40.8
9.44
3.83
1.82
3.0
9.5
63.2
52.0
46.4
3.2
5.2
3.6
2.6
5.6
3.8
2.8
15.2
6.29
3.04
17.0
7.04
3.40
12.2
4.99
2.39
13.7
5.60
2.68
10.7
4.33
2.06
12.0
4.87
2.31
3.4
5.9
4.1
3.0
18.9
7.81
3.77
15.3
6.24
2.98
13.4
5.43
2.58
3.6
6.3
4.3
3.2
20.9
8.63
4.16
16.9
6.90
3.30
14.9
6.02
2.86
3.8
6.6
4.6
3.3
23.0
9.48
4.57
18.7
7.60
3.63
16.5
6.64
3.15
4.0
6.9
4.8
3.5
25.1
10.4
4.99
20.5
8.33
3.97
18.1
7.29
3.45
4.2
7.3
5.0
3.7
27.4
11.3
5.43
22.3
9.09
4.33
19.8
7.97
3.77
4.4
7.6
5.3
3.9
29.7
12.2
5.89
24.3
9.87
4.71
21.6
8.67
4.10
4.6
8.0
5.5
4.1
32.1
13.2
6.36
26.3
10.7
5.09
23.4
9.40
4.44
4.8
8.3
5.7
4.2
34.6
14.2
6.85
28.5
11.5
5.49
25.3
10.2
4.80
5.0
8.7
6.0
4.4
37.2
15.3
7.35
30.6
12.4
5.91
27.3
11.0
5.17
5.5
9.6
6.6
4.8
44.0
18.1
8.68
36.4
14.7
7.01
32.6
13.0
6.15
6.0
7.2
5.3
21.1
10.1
17.3
8.19
15.3
7.20
6.5
7.8
5.7
24.3
11.6
19.9
9.45
17.7
8.34
7.0
8.4
6.2
27.7
13.2
22.8
10.8
20.3
9.55
7.5
9.0
6.6
31.2
15.0
25.9
12.2
23.1
10.8
8.0
9.6
7.0
35.0
16.8
29.1
13.7
26.1
8.5
7.5
18.6
15.3
12.2
13.7
9.0
7.9
20.6
17.0
15.2
9.5
8.4
22.7
18.8
16.8
10.0
8.8
24.9
20.6
18.4
11.0
9.7
29.5
24.5
22.0
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table values
shown in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
pressure loss, noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 6 / 15
9
Table
2B: Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
PipeWater
With/ 80%
Water / 20%
Table 2B:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 80%
20% Propylene
GlycolPropylene Glycol
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 20% Glycol
120°F (49°C) 20% Glycol
180°F (82°C) 20% Glycol
GPM
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1
0.5
0.4
0.3
0.1
0.11
0.05
0.02
<.01
0.11
0.04
0.02
<.01
0.09
0.04
0.02
<.01
2
1.1
0.7
0.5
0.3
0.47
0.18
0.05
0.02
0.36
0.14
0.06
0.02
0.30
0.12
0.05
0.01
3
1.6
1.1
0.8
0.4
0.93
0.36
0.17
0.05
0.72
0.28
0.13
0.04
0.62
0.24
0.11
0.03
4
2.1
1.4
1.0
0.6
1.52
0.59
0.27
0.08
1.20
0.46
0.21
0.06
1.03
0.39
0.18
0.05
5
2.7
1.8
1.3
0.7
2.24
0.87
0.39
0.11
1.77
0.68
0.31
0.09
1.53
0.58
0.26
0.07
6
3.2
2.1
1.5
0.9
3.06
1.19
0.54
0.15
2.45
0.94
0.42
0.12
2.13
0.81
0.36
0.10
7
3.7
2.5
1.8
1.0
4.01
1.55
0.70
0.20
3.22
1.23
0.55
0.15
2.81
1.07
0.48
0.13
8
4.3
2.9
2.0
1.2
5.06
1.95
0.88
0.25
4.09
1.56
0.70
0.19
3.58
1.35
0.61
0.17
9
4.8
3.2
2.3
1.3
6.22
2.39
1.08
0.30
5.05
1.92
0.86
0.24
4.44
1.68
0.75
0.21
10
5.3
3.6
2.6
1.5
7.48
2.88
1.30
0.36
6.10
2.32
1.04
0.29
5.38
2.03
0.90
0.25
11
5.9
3.9
2.8
1.6
8.84
3.40
1.54
0.43
7.24
2.75
1.23
0.34
6.41
2.41
1.07
0.29
12
6.4
4.3
3.1
1.8
10.3
3.96
1.79
0.50
8.47
3.21
1.44
0.40
7.52
2.82
1.26
0.34
13
6.9
4.6
3.3
1.9
11.9
4.56
2.06
0.57
9.79
3.71
1.66
0.46
8.71
3.27
1.45
0.40
14
7.5
5.0
3.6
2.1
13.5
5.19
2.34
0.65
11.2
4.24
1.90
0.52
9.99
3.74
1.66
0.45
15
8.0
5.4
3.8
2.2
15.3
5.86
2.64
0.73
12.7
4.80
2.14
0.59
11.3
4.24
1.88
0.51
16
8.5
5.7
4.1
2.4
17.2
6.57
2.96
0.82
14.3
5.39
2.41
0.66
12.8
4.78
2.12
0.57
17
9.1
6.1
4.4
2.5
19.1
7.31
3.29
0.91
16.0
6.02
2.68
0.74
14.3
5.34
2.36
0.64
18
9.6
21.2
17.7
15.9
19
6.4
4.6
2.7
8.09
3.64
1.01
6.8
4.9
2.8
8.91
4.01
1.11
6.68
2.98
0.81
7.36
3.28
0.90
5.93
2.62
0.71
6.56
2.90
0.78
20
7.1
5.1
3.0
9.76
4.39
1.21
8.08
3.60
0.98
7.21
3.18
0.86
22
7.9
5.6
3.3
11.6
5.19
1.43
9.62
4.27
1.16
8.60
3.79
1.02
24
8.6
6.1
3.6
13.5
6.06
1.67
11.3
5.00
1.36
10.1
4.45
1.20
26
9.3
6.7
3.9
15.6
6.98
1.93
13.1
5.79
1.57
11.7
5.16
1.38
1.58
28
7.2
4.2
7.97
2.19
6.62
1.80
5.91
30
7.7
4.5
9.01
2.48
7.51
2.03
6.72
1.80
32
8.2
4.8
10.1
2.78
8.45
2.29
7.58
2.02
34
8.7
5.1
11.3
3.09
9.44
2.55
8.48
2.26
36
9.2
5.4
12.5
3.42
10.5
2.83
9.44
2.51
38
9.7
5.7
13.8
3.77
11.6
3.12
10.4
40
6.0
4.13
3.42
2.77
3.05
42
6.3
4.50
3.74
3.34
44
6.6
4.89
4.07
3.64
46
6.9
5.30
4.42
3.95
48
7.2
5.72
4.77
4.27
50
7.5
6.15
5.14
4.61
52
7.8
6.60
5.53
4.96
54
8.1
7.06
5.92
5.32
56
8.4
7.54
6.33
5.69
58
8.7
8.03
6.75
6.07
60
9.0
8.53
7.18
6.47
65
9.7
9.85
8.32
7.51
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
– Flow velocity
8 and
fps (2.5 m/s) might
loss,of noise or erosion of the system components.
may result in excessive
of pipe.
feet of head,
– Table values
shown in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
pressure loss, noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
10
lee 2163, Page 7 / 15
855.681 en 03.2015
Table
PressureLoss
Loss
Metric-Sized
PEXaPipe
Carrier
PipeWater
With/ 20%
80%Propylene
Water / Glycol
20% Propylene Glycol
Table 2C:
2C: Pressure
for for
Metric-Sized
SDR11SDR11
REHAU REHAU
PEXa Carrier
with 80%
pressure loss in psi per 100 ft of pipe
Flow
ft/sec
Rate
60°F (16°C) 20% Glycol
120°F (49°C) 20% Glycol
180°F (82°C) 20% Glycol
GPM
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
0.1
0.4
0.1
<0.1
<0.1
0.60
0.01
<.01
<.01
0.25
<.01
<.01
<.01
0.14
<.01
<.01
<.01
0.2
0.8
0.1
0.1
<0.1
1.19
0.03
0.01
<.01
0.50
0.01
<.01
<.01
0.67
<.01
<.01
<.01
0.3
1.2
0.2
0.1
0.1
1.79
0.04
0.02
<.01
1.61
0.02
<.01
<.01
1.33
0.01
<.01
<.01
0.4
1.6
0.2
0.2
0.1
2.39
0.06
0.02
<.01
2.61
0.02
<.01
<.01
2.18
0.03
<.01
<.01
0.5
2.0
0.3
0.2
0.1
2.99
0.07
0.03
0.01
3.83
0.03
0.01
<.01
3.22
0.04
0.01
<.01
0.6
2.4
0.4
0.2
0.1
6.87
0.09
0.03
0.01
5.24
0.07
0.01
<.01
4.44
0.06
0.02
<.01
0.7
2.8
0.4
0.3
0.2
8.90
0.10
0.04
0.02
6.84
0.09
0.02
<.01
5.83
0.07
0.02
<.01
0.8
3.2
0.5
0.3
0.2
11.1
0.12
0.04
0.02
8.63
0.11
0.03
<.01
7.39
0.09
0.03
<.01
0.9
3.6
0.6
0.3
0.2
13.6
0.13
0.05
0.02
10.6
0.13
0.04
<.01
9.11
0.11
0.03
0.01
1.0
4.0
0.6
0.4
0.2
16.3
0.15
0.05
0.02
12.8
0.16
0.05
0.02
11.0
0.13
0.04
0.01
1.2
4.8
0.7
0.5
0.3
22.2
0.18
0.07
0.03
17.6
0.22
0.07
0.02
15.3
0.18
0.06
0.02
1.4
5.6
0.9
0.5
0.3
29.0
0.37
0.08
0.03
23.1
0.28
0.09
0.03
20.2
0.24
0.07
0.03
1.6
6.3
1.0
0.6
0.4
36.5
0.47
0.09
0.04
29.3
0.35
0.11
0.04
25.7
0.30
0.09
0.03
1.8
7.1
1.1
0.7
0.4
44.8
0.57
0.18
0.04
36.2
0.43
0.13
0.05
31.9
0.37
0.11
0.04
2.0
7.9
1.2
0.8
0.5
53.9
0.68
0.21
0.05
43.8
0.52
0.16
0.06
38.7
0.44
0.13
0.05
2.2
8.7
1.4
0.8
0.5
63.7
0.80
0.25
0.09
52.0
0.61
0.19
0.07
46.2
0.52
0.16
0.06
2.4
9.5
1.5
0.9
0.6
74.2
0.92
0.29
0.10
60.8
0.71
0.22
0.08
54.2
0.61
0.18
0.07
2.6
1.6
1.0
0.6
1.06
0.33
0.12
0.82
0.25
0.09
0.70
0.21
0.08
2.8
1.7
1.1
0.7
1.20
0.37
0.13
0.93
0.29
0.10
0.80
0.24
0.09
3.0
1.9
1.1
0.7
1.35
0.42
0.15
1.05
0.32
0.11
0.90
0.27
0.10
4.0
2.5
1.5
1.0
2.21
0.68
0.24
1.74
0.53
0.19
1.50
0.45
0.16
5.0
3.1
1.9
1.2
3.24
1.00
0.36
2.58
0.79
0.28
2.24
0.67
0.24
6.0
3.7
2.3
1.5
4.45
1.37
0.49
3.57
1.08
0.38
3.11
0.93
0.33
0.43
7.0
4.4
2.7
1.7
5.82
1.78
0.63
4.70
1.42
0.50
4.11
1.23
8.0
5.0
3.0
2.0
7.35
2.25
0.80
5.96
1.80
0.63
5.25
1.57
0.54
10.0
6.2
3.8
2.4
10.9
3.32
1.17
8.91
2.68
0.94
7.90
2.35
0.81
12.0
7.5
4.6
2.9
15.0
4.57
1.61
12.4
3.71
1.29
11.0
3.27
1.13
14.0
8.7
5.3
3.4
19.7
5.99
2.11
16.4
4.90
1.70
14.7
4.33
1.49
16.0
6.1
3.9
7.59
2.66
6.24
2.16
5.54
1.90
18.0
6.8
4.4
9.35
3.28
7.72
2.67
6.88
2.35
20.0
7.6
4.9
11.3
3.94
9.36
3.23
8.36
2.86
22.0
8.4
5.4
13.4
4.67
11.1
3.84
9.97
3.40
24.0
9.1
5.9
15.6
5.45
13.1
4.49
11.7
3.99
26.0
9.9
6.4
18.0
6.28
15.1
5.20
13.6
4.62
28.0
6.9
7.16
5.94
5.30
30.0
7.3
8.10
6.74
6.03
32.0
7.8
9.09
7.58
6.79
34.0
8.3
10.1
8.47
7.60
36.0
8.8
11.2
9.41
8.46
38.0
9.3
12.4
10.4
9.35
40.0
9.8
13.6
11.4
10.3
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
– Flow velocity
8 and
fps (2.5 m/s) might
loss,of noise or erosion of the system components.
may result in excessive
of pipe.
feet of head,
– Table values
shown in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
pressure loss, noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 8 / 15
11
Table
2D:Pressure
Pressure
Loss
Metric-Sized
PEXaPipe
Carrier
PipeWater
With/ 20%
80%Propylene
Water / Glycol
20% Propylene Glycol
Table 2D:
Loss
for for
Metric-Sized
SDR11SDR11
REHAU REHAU
PEXa Carrier
with 80%
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 20% Glycol
120°F (49°C) 20% Glycol
180°F (82°C) 20% Glycol
GPM
50
63
75
90
50
63
75
90
50
63
75
90
50
63
75
90
2
0.3
0.2
0.1
0.1
0.02
<.01
<.01
<.01
0.02
<.01
<.01
<.01
0.02
<.01
<.01
<.01
4
0.6
0.4
0.3
0.2
0.09
0.03
<.01
<.01
0.06
0.02
<.01
<.01
0.05
0.02
<.01
<.01
6
0.9
0.6
0.4
0.3
0.17
0.06
0.02
0.01
0.13
0.04
0.02
<.01
0.11
0.04
0.02
<.01
8
1.3
0.8
0.6
0.4
0.28
0.09
0.04
0.02
0.22
0.07
0.03
0.01
0.19
0.06
0.03
0.01
10
1.6
1.0
0.7
0.5
0.40
0.14
0.06
0.03
0.32
0.11
0.05
0.02
0.28
0.09
0.04
0.02
12
1.9
1.2
0.8
0.6
0.55
0.19
0.08
0.03
0.44
0.15
0.06
0.03
0.38
0.13
0.05
0.02
14
2.2
1.4
1.0
0.7
0.72
0.24
0.10
0.04
0.58
0.19
0.08
0.03
0.50
0.17
0.07
0.03
16
2.5
1.6
1.1
0.8
0.91
0.31
0.13
0.06
0.74
0.24
0.10
0.04
0.64
0.21
0.09
0.04
18
2.8
1.8
1.2
0.9
1.12
0.38
0.16
0.07
0.91
0.30
0.13
0.05
0.79
0.26
0.11
0.05
20
3.1
2.0
1.4
1.0
1.35
0.45
0.19
0.08
1.09
0.36
0.15
0.06
0.96
0.31
0.13
0.06
22
3.4
2.2
1.5
1.1
1.60
0.53
0.23
0.10
1.30
0.43
0.18
0.08
1.14
0.37
0.16
0.07
24
3.8
2.4
1.7
1.2
1.86
0.62
0.27
0.11
1.52
0.50
0.21
0.09
1.33
0.44
0.19
0.08
26
4.1
2.6
1.8
1.2
2.14
0.71
0.31
0.13
1.75
0.58
0.25
0.10
1.54
0.50
0.21
0.09
28
4.4
2.8
1.9
1.3
2.44
0.81
0.35
0.15
2.00
0.66
0.28
0.12
1.77
0.58
0.24
0.10
30
4.7
3.0
2.1
1.4
2.76
0.92
0.39
0.17
2.27
0.75
0.32
0.13
2.01
0.65
0.28
0.12
35
5.5
3.5
2.4
1.7
3.63
1.20
0.52
0.22
3.00
0.98
0.42
0.17
2.66
0.86
0.37
0.15
40
6.3
3.9
2.8
1.9
4.60
1.52
0.65
0.27
3.82
1.25
0.53
0.22
3.41
1.10
0.47
0.19
45
7.0
4.4
3.1
2.2
5.68
1.88
0.80
0.34
4.74
1.55
0.66
0.27
4.24
1.37
0.58
0.24
50
7.8
4.9
3.5
2.4
6.86
2.26
0.97
0.41
5.74
1.87
0.79
0.33
5.15
1.66
0.70
0.29
55
8.6
5.4
3.8
2.6
8.13
2.68
1.14
0.48
6.84
2.22
0.94
0.39
6.15
1.98
0.83
0.34
60
9.4
5.9
4.1
2.9
9.51
3.13
1.34
0.56
8.02
2.61
1.10
0.46
7.23
2.32
0.98
0.40
65
6.4
4.5
3.1
3.61
1.54
0.65
3.01
1.27
0.53
2.69
1.13
0.47
70
6.9
4.8
3.4
4.13
1.76
0.74
3.45
1.46
0.61
3.09
1.29
0.53
75
7.4
5.2
3.6
4.67
1.99
0.83
3.92
1.65
0.69
3.51
1.47
0.61
80
7.9
5.5
3.8
5.24
2.23
0.93
4.41
1.86
0.77
3.96
1.66
0.68
85
8.4
5.9
4.1
5.85
2.49
1.04
4.93
2.07
0.86
4.43
1.85
0.76
90
8.9
6.2
4.3
6.48
2.75
1.15
5.47
2.30
0.95
4.93
2.06
0.85
95
9.4
6.6
4.6
7.14
3.03
1.27
6.04
2.54
1.05
5.46
2.27
0.93
100
9.9
6.9
4.8
7.84
3.33
1.39
6.64
2.79
1.15
6.01
2.50
1.03
105
7.3
5.0
3.63
1.52
3.05
1.26
2.74
1.12
110
7.6
5.3
3.95
1.65
3.32
1.37
2.99
1.22
115
7.9
5.5
4.28
1.78
3.60
1.49
3.24
1.33
120
8.3
5.8
4.62
1.92
3.90
1.61
3.51
1.44
130
9.0
6.2
5.33
2.22
4.52
1.86
4.08
1.67
140
9.7
6.7
6.10
2.54
5.18
2.13
4.69
1.91
150
7.2
2.87
2.42
2.18
160
7.7
3.23
2.72
2.45
170
8.2
3.60
3.05
2.75
180
8.7
3.99
3.38
3.06
190
9.1
4.40
3.74
3.38
200
9.6
4.83
4.11
3.72
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
– Flow velocity
8 and
fps (2.5 m/s) might
loss,of noise or erosion of the system components.
may result in excessive
of pipe.
feet of head,
– Table values
shown in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
pressure loss, noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express
pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
12
lee 2163, Page 9 / 15
855.681 en 03.2015
Table
2E: Pressure Loss for Metric-Sized SDR11 REHAU PEXa Carrier Pipe With 80% Water / 20% Propylene Glycol
Table 2E:
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 20% Glycol
120°F (49°C) 20% Glycol
180°F (82°C) 20% Glycol
GPM
110
125
140
160
110
125
140
160
110
125
140
160
110
125
140
160
5
0.2
0.1
0.1
0.1
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
10
0.3
0.2
0.2
0.2
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
15
0.5
0.4
0.3
0.2
0.02
0.01
<.01
<.01
0.02
<.01
<.01
<.01
0.01
<.01
<.01
<.01
20
0.6
0.5
0.4
0.3
0.03
0.02
0.01
<.01
0.03
0.01
<.01
<.01
0.02
0.01
<.01
<.01
25
0.8
0.6
0.5
0.4
0.05
0.03
0.01
<.01
0.04
0.02
0.01
<.01
0.03
0.02
0.01
<.01
30
1.0
0.7
0.6
0.5
0.06
0.04
0.02
0.01
0.05
0.03
0.02
<.01
0.04
0.02
0.01
<.01
40
1.3
1.0
0.8
0.6
0.11
0.06
0.03
0.02
0.08
0.05
0.03
0.01
0.07
0.04
0.02
0.01
50
1.6
1.2
1.0
0.8
0.16
0.09
0.05
0.03
0.13
0.07
0.04
0.02
0.11
0.06
0.03
0.02
60
1.9
1.5
1.2
0.9
0.22
0.12
0.07
0.04
0.17
0.09
0.05
0.03
0.15
0.08
0.05
0.03
70
2.3
1.7
1.4
1.1
0.28
0.15
0.09
0.05
0.23
0.12
0.07
0.04
0.20
0.11
0.06
0.03
80
2.6
2.0
1.6
1.2
0.36
0.19
0.11
0.06
0.29
0.16
0.09
0.05
0.26
0.14
0.08
0.04
90
2.9
2.2
1.8
1.4
0.44
0.24
0.14
0.07
0.36
0.20
0.11
0.06
0.32
0.17
0.10
0.05
100
3.2
2.5
2.0
1.5
0.53
0.29
0.17
0.09
0.44
0.24
0.14
0.07
0.39
0.21
0.12
0.06
110
3.5
2.7
2.2
1.7
0.63
0.34
0.20
0.11
0.52
0.28
0.16
0.09
0.46
0.25
0.14
0.08
120
3.9
3.0
2.4
1.8
0.73
0.40
0.23
0.12
0.61
0.33
0.19
0.10
0.54
0.29
0.17
0.09
130
4.2
3.2
2.6
2.0
0.85
0.46
0.27
0.14
0.70
0.38
0.22
0.12
0.63
0.34
0.19
0.10
140
4.5
3.5
2.8
2.1
0.97
0.52
0.30
0.16
0.81
0.43
0.25
0.13
0.72
0.38
0.22
0.12
150
4.8
3.7
3.0
2.3
1.09
0.59
0.34
0.18
0.91
0.49
0.28
0.15
0.81
0.44
0.25
0.13
160
5.1
4.0
3.2
2.4
1.23
0.67
0.38
0.20
1.03
0.55
0.32
0.17
0.92
0.49
0.28
0.15
170
5.5
4.2
3.4
2.6
1.37
0.74
0.43
0.23
1.15
0.62
0.36
0.19
1.03
0.55
0.32
0.17
180
5.8
4.5
3.6
2.7
1.52
0.82
0.47
0.25
1.27
0.69
0.39
0.21
1.14
0.61
0.35
0.18
0.20
190
6.1
4.7
3.8
2.9
1.67
0.91
0.52
0.28
1.41
0.76
0.43
0.23
1.26
0.67
0.39
200
6.4
5.0
4.0
3.0
1.83
0.99
0.57
0.30
1.54
0.83
0.48
0.25
1.39
0.74
0.42
0.22
225
7.2
5.6
4.5
3.4
2.27
1.23
0.71
0.38
1.92
1.03
0.59
0.31
1.72
0.92
0.53
0.28
250
8.0
6.2
5.0
3.8
2.74
1.48
0.86
0.45
2.33
1.25
0.72
0.38
2.10
1.12
0.64
0.34
275
8.8
6.9
5.5
4.2
3.26
1.76
1.02
0.54
2.77
1.49
0.85
0.45
2.51
1.34
0.76
0.40
300
9.7
3.82
3.26
2.95
325
7.5
6.0
4.6
8.1
6.4
4.9
2.06
1.19
0.63
2.38
1.37
0.73
1.75
1.00
0.53
2.02
1.16
0.61
1.57
0.90
0.47
1.83
1.04
0.54
350
8.7
6.9
5.3
2.72
1.57
0.83
2.32
1.33
0.70
2.10
1.20
0.62
375
9.4
7.4
5.7
3.09
1.78
0.94
2.64
1.51
0.79
2.39
1.36
0.71
400
10.0
7.9
6.1
3.47
2.00
1.05
2.97
1.70
0.89
2.70
8.4
6.5
2.23
1.18
1.90
1.00
425
1.53
0.80
1.72
0.90
450
8.9
6.9
2.47
1.31
2.11
1.11
1.91
1.00
475
9.4
7.2
2.73
1.44
2.33
1.22
2.12
1.10
500
9.9
7.6
3.00
1.58
2.57
1.34
2.33
525
8.0
1.73
1.47
1.21
1.33
550
8.4
1.88
1.60
1.45
575
8.8
2.04
1.74
1.58
600
9.1
2.20
1.88
1.71
625
9.5
2.37
2.03
1.84
650
9.9
2.54
2.18
1.98
Flow Velocity above
Shown is pressure
To express
loss in
– Flow velocity above 8 fps (2.5 m/s) might result in excessive pressurepressure
loss, noise
or erosion of the system components.
considered excessive and
psi per 100 ft
terms of
– Table values
in pressure loss units
of psi per 100 ft (30.5 m) offeetpipe.
may resultshown
in excessive
of pipe.
of head,
pressure loss, noise or
Example:
for 200 lineal ft of pipe, double the value listed in this table.multiply the value
erosion of system
Example: for 200
listed by 2.307.
– To express
pressure loss in terms of feet
head,
components.
linealof
ft of
pipe, multiply the table value by 2.307.
Example: 1 psi =
Example: 1 psi = 2.307 ft of head. double the value
8 feet per second may be
loss in units of
listed in this table.
2.20150309-pressureloss_raupex_rautherm(emailcopyonly) (1).xlsx
855.681 en 03.2015
2.307 ft of head
lee 2163, Page 1 / 1
13
Table
3A:Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
PipeWater
With/ 50%
50%Propylene
Water / 50%
Table 3A:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 50%
GlycolPropylene Glyco
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 50% Glycol
120°F (49°C) 50% Glycol
180°F (82°C) 50% Glycol
GPM
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
3/8"
1/2"
5/8"
3/4"
0.1
0.3
0.2
0.1
0.1
1.31
0.40
0.19
0.10
0.38
0.12
0.06
0.03
0.17
0.05
0.03
0.01
0.2
0.6
0.3
0.2
0.2
2.63
0.80
0.38
0.21
0.77
0.23
0.11
0.06
0.35
0.11
0.05
0.03
0.3
0.9
0.5
0.4
0.3
3.94
1.20
0.57
0.31
1.15
0.35
0.17
0.09
0.96
0.16
0.08
0.04
0.4
1.3
0.7
0.5
0.4
5.26
1.60
0.76
0.41
1.53
0.47
0.22
0.12
1.56
0.39
0.10
0.05
0.5
1.6
0.9
0.6
0.4
6.57
2.00
0.95
0.51
1.92
0.58
0.28
0.15
2.27
0.56
0.23
0.07
0.6
1.9
1.0
0.7
0.5
7.89
2.39
1.14
0.62
2.30
0.70
0.33
0.18
3.10
0.76
0.32
0.16
0.7
2.2
1.2
0.8
0.6
9.20
2.79
1.33
0.72
5.23
0.82
0.39
0.21
4.04
0.99
0.41
0.20
0.8
2.5
1.4
1.0
0.7
10.5
3.19
1.52
0.82
6.54
0.93
0.44
0.24
5.09
1.24
0.52
0.25
0.9
2.8
1.6
1.1
0.8
11.8
3.59
1.71
0.92
7.98
1.97
0.50
0.27
6.24
1.52
0.63
0.31
1.0
3.2
1.7
1.2
0.9
13.1
3.99
1.90
1.03
9.54
2.35
0.99
0.30
7.50
1.82
0.76
0.37
1.2
3.8
2.1
1.4
1.1
15.8
4.79
2.28
1.23
13.0
3.19
1.34
0.65
10.3
2.49
1.03
0.50
1.4
4.4
2.4
1.7
1.2
18.4
5.59
2.66
1.44
16.9
4.14
1.73
0.84
13.5
3.25
1.35
0.65
1.6
5.0
2.8
1.9
1.4
21.0
6.39
3.04
1.64
21.3
5.20
2.17
1.05
17.1
4.10
1.69
0.82
1.8
5.7
3.1
2.2
1.6
23.7
7.18
3.42
1.85
26.1
6.36
2.65
1.29
21.1
5.04
2.08
1.00
2.0
6.3
3.5
2.4
1.8
26.3
7.98
3.80
2.05
31.3
7.61
3.17
1.54
25.4
6.06
2.50
1.20
2.2
6.9
3.8
2.6
1.9
53.8
8.78
4.18
2.26
37.0
8.97
3.73
1.81
30.1
7.17
2.95
1.42
2.4
7.6
4.2
2.9
2.1
62.3
9.58
4.56
2.46
43.1
10.4
4.32
2.09
35.2
8.36
3.43
1.65
2.6
8.2
4.5
3.1
2.3
71.2
10.4
4.94
2.67
49.5
12.0
4.96
2.40
40.7
9.63
3.95
1.90
2.8
8.8
4.9
3.4
2.5
80.7
20.0
5.32
2.88
56.4
13.6
5.63
2.72
46.5
11.0
4.50
2.16
3.0
9.5
90.6
63.7
52.7
3.2
5.2
3.6
2.6
5.6
3.8
2.8
22.4
5.70
3.08
25.0
6.08
3.29
15.3
6.34
3.07
17.2
7.09
3.42
12.4
5.08
2.44
13.9
5.70
2.73
3.4
5.9
4.1
3.0
27.6
11.6
3.49
19.1
7.87
3.80
15.5
6.34
3.04
3.6
6.3
4.3
3.2
30.4
12.7
3.70
21.1
8.69
4.19
17.2
7.02
3.36
3.8
6.6
4.6
3.3
33.3
13.9
3.90
23.1
9.55
4.60
18.9
7.73
3.69
4.0
6.9
4.8
3.5
36.3
15.2
7.41
25.3
10.4
5.03
20.8
8.46
4.04
4.2
7.3
5.0
3.7
39.4
16.5
8.03
27.6
11.4
5.47
22.7
9.23
4.41
4.4
7.6
5.3
3.9
42.6
17.8
8.68
29.9
12.3
5.93
24.6
10.0
4.79
4.6
8.0
5.5
4.1
46.0
19.2
9.35
32.4
13.3
6.41
26.7
10.9
5.18
4.8
8.3
5.7
4.2
49.4
20.6
10.0
34.9
14.3
6.90
28.8
11.7
5.59
5.0
8.7
6.0
4.4
52.9
22.1
10.7
37.5
15.4
7.41
31.0
12.6
6.01
5.5
9.6
6.6
4.8
62.2
26.0
12.6
44.4
18.2
8.75
36.9
15.0
7.12
6.0
7.2
5.3
30.1
14.6
21.2
10.2
17.5
8.31
6.5
7.8
5.7
34.5
16.7
24.4
11.7
20.2
9.60
7.0
8.4
6.2
39.1
19.0
27.9
13.3
23.1
11.0
7.5
9.0
6.6
44.0
21.3
31.5
15.1
26.2
12.4
8.0
9.6
7.0
49.1
23.8
35.3
16.9
29.4
8.5
7.5
26.4
18.8
13.9
15.6
9.0
7.9
29.1
20.8
17.2
9.5
8.4
31.9
22.9
19.0
10.0
8.8
34.8
25.0
20.9
11.0
9.7
41.0
29.7
24.8
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
values loss,
shown
in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
14
lee 2163, Page 11 / 15
855.681 en 03.2015
Table
3B:Pressure
Pressure
Loss
Inch-Sized
PEXaPipe
Carrier
PipeWater
With/ 50%
50%Propylene
Water / Glycol
50% Propylene Glycol
Table 3B:
Loss
for for
Inch-Sized
SDR9 SDR9
REHAUREHAU
PEXa Carrier
with 50%
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 50% Glycol
120°F (49°C) 50% Glycol
180°F (82°C) 50% Glycol
GPM
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1"
1-1/4"
1-1/2"
2"
1
0.5
0.4
0.3
0.1
0.38
0.17
0.09
0.03
0.11
0.05
0.03
<.01
0.11
0.04
0.02
<.01
2
1.1
0.7
0.5
0.3
0.75
0.34
0.17
0.06
0.47
0.19
0.05
0.02
0.37
0.14
0.06
0.02
3
1.6
1.1
0.8
0.4
1.13
0.51
0.26
0.09
0.94
0.37
0.17
0.05
0.74
0.29
0.13
0.04
4
2.1
1.4
1.0
0.6
1.51
0.68
0.35
0.12
1.54
0.60
0.27
0.08
1.22
0.47
0.21
0.06
5
2.7
1.8
1.3
0.7
3.33
0.85
0.43
0.15
2.25
0.87
0.40
0.11
1.80
0.69
0.31
0.09
6
3.2
2.1
1.5
0.9
4.51
1.01
0.52
0.18
3.09
1.20
0.54
0.15
2.49
0.96
0.43
0.12
7
3.7
2.5
1.8
1.0
5.84
2.29
0.61
0.21
4.04
1.56
0.71
0.20
3.27
1.25
0.57
0.16
8
4.3
2.9
2.0
1.2
7.32
2.86
1.31
0.24
5.10
1.97
0.89
0.25
4.15
1.59
0.71
0.20
9
4.8
3.2
2.3
1.3
8.93
3.49
1.60
0.27
6.26
2.41
1.09
0.31
5.12
1.95
0.88
0.24
10
5.3
3.6
2.6
1.5
10.7
4.17
1.91
0.54
7.53
2.90
1.31
0.37
6.19
2.36
1.06
0.29
11
5.9
3.9
2.8
1.6
12.6
4.89
2.24
0.64
8.91
3.43
1.55
0.43
7.34
2.79
1.25
0.35
12
6.4
4.3
3.1
1.8
14.6
5.67
2.59
0.73
10.4
3.99
1.80
0.50
8.59
3.26
1.46
0.40
13
6.9
4.6
3.3
1.9
16.7
6.50
2.97
0.84
12.0
4.59
2.07
0.58
9.92
3.77
1.69
0.46
14
7.5
5.0
3.6
2.1
19.0
7.37
3.36
0.95
13.6
5.23
2.36
0.66
11.3
4.30
1.93
0.53
15
8.0
5.4
3.8
2.2
21.3
8.29
3.78
1.07
15.4
5.91
2.66
0.74
12.9
4.87
2.18
0.60
16
8.5
5.7
4.1
2.4
23.9
9.26
4.22
1.19
17.3
6.62
2.98
0.83
14.5
5.47
2.44
0.67
17
9.1
6.1
4.4
2.5
26.5
10.3
4.68
1.32
19.3
7.37
3.32
0.92
16.1
6.10
2.73
0.75
18
9.6
29.2
21.3
17.9
19
6.4
4.6
2.7
6.8
4.9
2.8
11.3
5.16
1.45
8.15
3.67
1.02
12.4
5.66
1.59
8.97
4.04
1.12
6.77
3.02
0.83
7.46
3.33
0.91
20
7.1
5.1
3.0
13.6
6.18
1.74
9.83
4.42
1.22
8.19
3.65
1.00
22
7.9
5.6
3.3
16.0
7.27
2.04
11.6
5.23
1.45
9.73
4.33
1.18
24
8.6
6.1
3.6
18.6
8.45
2.37
13.6
6.10
1.68
11.4
5.07
1.38
26
9.3
6.7
3.9
21.4
9.70
2.72
15.7
7.03
1.94
13.2
5.86
1.60
1.82
28
7.2
4.2
11.0
3.09
8.03
2.21
6.71
30
7.7
4.5
12.4
3.47
9.08
2.50
7.60
2.06
32
8.2
4.8
13.9
3.88
10.2
2.80
8.55
2.32
34
8.7
5.1
15.4
4.31
11.4
3.12
9.55
2.59
36
9.2
5.4
17.0
4.76
12.6
3.45
10.6
2.87
38
9.7
5.7
18.7
5.22
13.9
3.80
11.7
40
6.0
5.71
4.16
3.16
3.47
42
6.3
6.21
4.54
3.79
44
6.6
6.73
4.93
4.12
46
6.9
7.27
5.34
4.47
48
7.2
7.83
5.76
4.83
50
7.5
8.40
6.19
5.20
52
7.8
9.00
6.64
5.59
54
8.1
9.61
7.11
5.99
56
8.4
10.2
7.59
6.40
58
8.7
10.9
8.08
6.82
60
9.0
11.5
8.59
7.26
65
9.7
13.3
9.92
8.41
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressure
terms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
values loss,
shown
in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 12 / 15
15
Table
PressureLoss
Loss
Metric-Sized
PEXaPipe
Carrier
PipeWater
With/ 50%
50%Propylene
Water / Glycol
50% Propylene Glycol
Table 3C:
3C: Pressure
for for
Metric-Sized
SDR11SDR11
REHAU REHAU
PEXa Carrier
with 50%
pressure loss in psi per 100 ft of pipe
Flow
ft/sec
Rate
60°F (16°C) 50% Glycol
120°F (49°C) 50% Glycol
180°F (82°C) 50% Glycol
GPM
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
10.1
25
32
40
0.1
0.4
0.1
<0.1
<0.1
2.08
0.05
0.02
<.01
0.61
0.02
<.01
<.01
0.28
<.01
<.01
<.01
0.2
0.8
0.1
0.1
<0.1
4.17
0.10
0.04
0.02
1.22
0.03
0.01
<.01
0.55
0.01
<.01
<.01
0.3
1.2
0.2
0.1
0.1
6.25
0.15
0.06
0.02
1.82
0.05
0.02
<.01
1.65
0.02
<.01
<.01
0.4
1.6
0.2
0.2
0.1
8.33
0.21
0.08
0.03
2.43
0.06
0.02
<.01
2.68
0.03
0.01
<.01
0.5
2.0
0.3
0.2
0.1
10.4
0.26
0.10
0.04
3.04
0.08
0.03
0.01
3.92
0.03
0.01
<.01
0.6
2.4
0.4
0.2
0.1
12.5
0.31
0.11
0.05
6.93
0.09
0.03
0.01
5.36
0.04
0.02
<.01
0.7
2.8
0.4
0.3
0.2
14.6
0.36
0.13
0.06
8.97
0.11
0.04
0.02
6.99
0.09
0.02
<.01
0.8
3.2
0.5
0.3
0.2
16.7
0.41
0.15
0.06
11.2
0.12
0.04
0.02
8.81
0.11
0.02
<.01
0.9
3.6
0.6
0.3
0.2
18.8
0.46
0.17
0.07
13.7
0.14
0.05
0.02
10.8
0.14
0.04
<.01
1.0
4.0
0.6
0.4
0.2
20.8
0.52
0.19
0.08
16.4
0.15
0.06
0.02
13.0
0.16
0.05
0.01
1.2
4.8
0.7
0.5
0.3
25.0
0.62
0.23
0.10
22.4
0.18
0.07
0.03
17.9
0.22
0.07
0.02
1.4
5.6
0.9
0.5
0.3
29.2
0.72
0.27
0.11
29.2
0.38
0.08
0.03
23.5
0.29
0.09
0.03
1.6
6.3
1.0
0.6
0.4
33.3
0.82
0.31
0.13
36.8
0.47
0.09
0.04
29.8
0.36
0.11
0.04
1.8
7.1
1.1
0.7
0.4
37.5
0.93
0.34
0.14
45.2
0.57
0.18
0.04
36.8
0.44
0.14
0.05
2.0
7.9
1.2
0.8
0.5
78.7
1.03
0.38
0.16
54.3
0.68
0.21
0.05
44.4
0.53
0.16
0.06
2.2
8.7
1.4
0.8
0.5
92.3
1.13
0.42
0.17
64.1
0.80
0.25
0.09
52.7
0.63
0.19
0.07
2.4
9.5
1.5
0.9
0.6
106.9
1.24
0.46
0.19
74.7
0.93
0.29
0.10
61.7
0.73
0.22
0.08
2.6
1.6
1.0
0.6
1.34
0.50
0.21
1.07
0.33
0.12
0.84
0.26
0.09
2.8
1.7
1.1
0.7
1.44
0.53
0.22
1.21
0.38
0.13
0.95
0.29
0.10
3.0
1.9
1.1
0.7
1.55
0.57
0.24
1.36
0.42
0.15
1.07
0.33
0.12
4.0
2.5
1.5
1.0
2.06
0.76
0.32
2.22
0.69
0.25
1.77
0.54
0.19
5.0
3.1
1.9
1.2
4.80
0.95
0.40
3.27
1.01
0.36
2.63
0.80
0.28
6.0
3.7
2.3
1.5
6.51
2.04
0.48
4.48
1.38
0.49
3.63
1.10
0.39
0.51
7.0
4.4
2.7
1.7
8.44
2.63
0.56
5.86
1.80
0.64
4.77
1.45
8.0
5.0
3.0
2.0
10.6
3.29
1.18
7.40
2.27
0.80
6.06
1.83
0.64
10.0
6.2
3.8
2.4
15.4
4.80
1.72
11.0
3.34
1.18
9.04
2.72
0.95
12.0
7.5
4.6
2.9
21.1
6.53
2.33
15.1
4.60
1.62
12.6
3.77
1.32
14.0
8.7
5.3
3.4
27.5
8.49
3.03
19.9
6.04
2.12
16.6
4.97
1.73
16.0
6.1
3.9
10.7
3.80
7.64
2.68
6.32
2.20
18.0
6.8
4.4
13.1
4.64
9.41
3.30
7.83
2.71
20.0
7.6
4.9
15.7
5.56
11.4
3.97
9.47
3.28
22.0
8.4
5.4
18.5
6.55
13.5
4.70
11.3
3.89
24.0
9.1
5.9
21.4
7.60
15.7
5.49
13.2
4.55
26.0
9.9
6.4
24.6
8.73
18.1
6.32
15.3
5.26
28.0
6.9
9.92
7.21
6.02
30.0
7.3
11.2
8.16
6.82
32.0
7.8
12.5
9.15
7.67
34.0
8.3
13.9
10.2
8.57
36.0
8.8
15.3
11.3
9.51
38.0
9.3
16.8
12.4
10.5
40.0
9.8
18.4
13.6
11.5
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressureterms
– Flow velocity
8 and
fps (2.5 m/s) might
loss,of noise or erosion of the system components.
may result in excessive
of pipe.
feet of head,
– Table values
shown in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
pressure loss, noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
16
lee 2163, Page 13 / 15
855.681 en 03.2015
Table
3D:Pressure
Pressure
Loss
Metric-Sized
REHAU
PEXa
Carrier
Pipe
With
50%
Water /Glycol
50% Propylene Glycol
Table 3D:
Loss
for for
Metric-Sized
SDR11 SDR11
REHAU PEXa
Carrier
Pipe
with 50%
Water
/ 50%
Propylene
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 50% Glycol
120°F (49°C) 50% Glycol
180°F (82°C) 50% Glycol
GPM
50
63
75
90
50
63
75
90
50
63
75
90
50
63
75
90
2
0.3
0.2
0.1
0.1
0.06
0.03
0.01
<.01
0.02
<.01
<.01
<.01
0.02
<.01
<.01
<.01
4
0.6
0.4
0.3
0.2
0.13
0.05
0.03
0.01
0.09
0.03
<.01
<.01
0.07
0.02
<.01
<.01
6
0.9
0.6
0.4
0.3
0.19
0.08
0.04
0.02
0.17
0.06
0.03
0.01
0.13
0.04
0.02
<.01
8
1.3
0.8
0.6
0.4
0.26
0.10
0.05
0.02
0.28
0.09
0.04
0.02
0.22
0.07
0.03
0.01
10
1.6
1.0
0.7
0.5
0.60
0.13
0.06
0.03
0.41
0.14
0.06
0.03
0.33
0.11
0.05
0.02
12
1.9
1.2
0.8
0.6
0.82
0.28
0.08
0.04
0.56
0.19
0.08
0.03
0.45
0.15
0.06
0.03
14
2.2
1.4
1.0
0.7
1.06
0.36
0.16
0.04
0.73
0.24
0.11
0.04
0.59
0.20
0.08
0.04
16
2.5
1.6
1.1
0.8
1.32
0.45
0.20
0.05
0.92
0.31
0.13
0.06
0.75
0.25
0.11
0.04
18
2.8
1.8
1.2
0.9
1.62
0.55
0.24
0.10
1.13
0.38
0.16
0.07
0.92
0.31
0.13
0.06
20
3.1
2.0
1.4
1.0
1.93
0.65
0.28
0.12
1.36
0.45
0.20
0.08
1.11
0.37
0.16
0.07
22
3.4
2.2
1.5
1.1
2.27
0.77
0.33
0.14
1.61
0.54
0.23
0.10
1.32
0.44
0.19
0.08
0.09
24
3.8
2.4
1.7
1.2
2.64
0.89
0.39
0.17
1.88
0.62
0.27
0.11
1.54
0.51
0.22
26
4.1
2.6
1.8
1.2
3.02
1.02
0.44
0.19
2.16
0.72
0.31
0.13
1.78
0.59
0.25
0.11
28
4.4
2.8
1.9
1.3
3.43
1.16
0.50
0.21
2.46
0.82
0.35
0.15
2.03
0.67
0.29
0.12
30
4.7
3.0
2.1
1.4
3.87
1.30
0.56
0.24
2.78
0.92
0.40
0.17
2.30
0.76
0.32
0.14
35
5.5
3.5
2.4
1.7
5.04
1.69
0.73
0.31
3.66
1.21
0.52
0.22
3.04
1.00
0.42
0.18
40
6.3
3.9
2.8
1.9
6.35
2.13
0.92
0.39
4.64
1.53
0.66
0.28
3.87
1.27
0.54
0.23
45
7.0
4.4
3.1
2.2
7.79
2.61
1.13
0.48
5.72
1.89
0.81
0.34
4.79
1.57
0.67
0.28
50
7.8
4.9
3.5
2.4
9.35
3.13
1.35
0.57
6.90
2.28
0.97
0.41
5.81
1.90
0.80
0.34
55
8.6
5.4
3.8
2.6
11.0
3.69
1.59
0.68
8.19
2.70
1.15
0.48
6.91
2.25
0.95
0.40
60
9.4
12.9
9.58
8.11
0.47
5.9
4.1
2.9
4.30
1.85
0.78
3.15
1.35
0.56
2.64
1.12
65
6.4
4.5
3.1
4.94
2.13
0.90
3.64
1.55
0.65
3.05
1.29
0.54
70
6.9
4.8
3.4
5.62
2.42
1.02
4.16
1.77
0.74
3.49
1.48
0.61
75
7.4
5.2
3.6
6.34
2.73
1.15
4.70
2.00
0.84
3.96
1.67
0.70
80
7.9
5.5
3.8
7.10
3.05
1.29
5.28
2.25
0.94
4.46
1.88
0.78
85
8.4
5.9
4.1
7.89
3.39
1.43
5.89
2.50
1.05
4.98
2.10
0.87
90
8.9
6.2
4.3
8.72
3.75
1.58
6.52
2.77
1.16
5.53
2.33
0.97
95
9.4
6.6
4.6
9.59
4.12
1.74
7.19
3.05
1.28
6.11
2.57
1.07
100
9.9
6.9
4.8
10.5
4.50
1.90
7.89
3.35
1.40
6.71
2.82
1.17
105
7.3
5.0
4.90
2.07
3.66
1.53
3.09
1.28
110
7.6
5.3
5.32
2.24
3.97
1.66
3.36
1.39
115
7.9
5.5
5.75
2.42
4.31
1.80
3.64
1.51
120
8.3
5.8
6.20
2.61
4.65
1.94
3.94
1.63
130
9.0
6.2
7.13
3.00
5.37
2.24
4.56
1.88
140
9.7
6.7
8.13
3.42
6.14
2.56
5.23
2.16
150
7.2
3.86
2.89
2.45
160
7.7
4.32
3.25
2.75
170
8.2
4.81
3.62
3.08
180
8.7
5.32
4.02
3.42
190
9.1
5.85
4.43
3.78
200
9.6
6.41
4.86
4.15
Flow Velocity above
Shown is pressure
To express
8 feet per second may be
loss in units of
pressure loss in
consideredabove
excessive
psi perresult
100 ft in excessive pressure
terms
of noise or erosion of the system components.
– Flow velocity
8 and
fps (2.5 m/s) might
loss,
may result in excessive
of pipe.
feet of head,
– Table pressure
values loss,
shown
in pressure loss units of psi per 100 ft (30.5 m) ofmultiply
pipe.the value
noise or
erosion
of
system
Example:
for
200
listed
Example: for 200 lineal ft of pipe, double the value listed in this table. by 2.307.
components.
lineal ft of pipe,
– To express pressure loss in terms of feet
of head, multiply the table value
by 2.307.
double the value
Example: 1 psi =
listed
in
this
table.
2.307
ft
of head
Example: 1 psi = 2.307 ft of head.
pressureloss_raupex_rautherm_2013.04-emailonly.xlsx
855.681 en 03.2015
lee 2163, Page 14 / 15
17
Table
3E: Pressure Loss for Metric-Sized SDR11 REHAU PEXa Carrier Pipe With 50% Water / 50% Propylene Glycol
Table 3E:
Flow
Flow Velocity
Rate
ft/sec
pressure loss in psi per 100 ft of pipe
60°F (16°C) 50% Glycol
120°F (49°C) 50% Glycol
180°F (82°C) 50% Glycol
GPM
110
125
140
160
110
125
140
160
110
125
140
160
110
125
140
160
5
0.2
0.1
0.1
0.1
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
10
0.3
0.2
0.2
0.2
0.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
<.01
15
0.5
0.4
0.3
0.2
0.02
0.01
<.01
<.01
0.02
0.01
<.01
<.01
0.02
<.01
<.01
<.01
20
0.6
0.5
0.4
0.3
0.03
0.02
0.01
<.01
0.03
0.02
0.01
<.01
0.03
0.01
<.01
<.01
25
0.8
0.6
0.5
0.4
0.07
0.04
0.01
<.01
0.05
0.03
0.02
<.01
0.04
0.02
0.01
<.01
30
1.0
0.7
0.6
0.5
0.09
0.05
0.03
0.02
0.06
0.04
0.02
0.01
0.05
0.03
0.02
<.01
40
1.3
1.0
0.8
0.6
0.15
0.08
0.05
0.03
0.11
0.06
0.03
0.02
0.09
0.05
0.03
0.01
50
1.6
1.2
1.0
0.8
0.22
0.12
0.07
0.04
0.16
0.09
0.05
0.03
0.13
0.07
0.04
0.02
60
1.9
1.5
1.2
0.9
0.30
0.17
0.10
0.05
0.22
0.12
0.07
0.04
0.18
0.10
0.06
0.03
70
2.3
1.7
1.4
1.1
0.40
0.22
0.13
0.07
0.28
0.15
0.09
0.05
0.23
0.13
0.07
0.04
80
2.6
2.0
1.6
1.2
0.50
0.27
0.16
0.09
0.36
0.20
0.11
0.06
0.30
0.16
0.09
0.05
90
2.9
2.2
1.8
1.4
0.61
0.33
0.20
0.10
0.44
0.24
0.14
0.07
0.37
0.20
0.11
0.06
100
3.2
2.5
2.0
1.5
0.73
0.40
0.23
0.13
0.53
0.29
0.17
0.09
0.44
0.24
0.14
0.07
110
3.5
2.7
2.2
1.7
0.87
0.47
0.28
0.15
0.63
0.34
0.20
0.11
0.53
0.29
0.16
0.09
120
3.9
3.0
2.4
1.8
1.01
0.55
0.32
0.17
0.74
0.40
0.23
0.12
0.62
0.33
0.19
0.10
130
4.2
3.2
2.6
2.0
1.16
0.63
0.37
0.20
0.85
0.46
0.27
0.14
0.71
0.39
0.22
0.12
140
4.5
3.5
2.8
2.1
1.32
0.72
0.42
0.22
0.97
0.53
0.31
0.16
0.82
0.44
0.25
0.13
150
4.8
3.7
3.0
2.3
1.49
0.81
0.47
0.25
1.10
0.60
0.35
0.18
0.92
0.50
0.29
0.15
160
5.1
4.0
3.2
2.4
1.66
0.91
0.53
0.28
1.24
0.67
0.39
0.21
1.04
0.56
0.32
0.17
170
5.5
4.2
3.4
2.6
1.85
1.01
0.59
0.31
1.38
0.75
0.43
0.23
1.16
0.63
0.36
0.19
180
5.8
4.5
3.6
2.7
2.05
1.12
0.65
0.35
1.53
0.83
0.48
0.25
1.29
0.69
0.40
0.21
0.23
190
6.1
4.7
3.8
2.9
2.25
1.23
0.71
0.38
1.68
0.91
0.53
0.28
1.42
0.77
0.44
200
6.4
5.0
4.0
3.0
2.46
1.34
0.78
0.42
1.85
1.00
0.58
0.31
1.56
0.84
0.48
0.26
225
7.2
5.6
4.5
3.4
3.03
1.65
0.96
0.51
2.28
1.24
0.71
0.38
1.94
1.04
0.60
0.32
250
8.0
6.2
5.0
3.8
3.65
1.99
1.15
0.61
2.76
1.49
0.86
0.46
2.35
1.26
0.73
0.38
275
8.8
6.9
5.5
4.2
4.32
2.35
1.36
0.73
3.28
1.77
1.02
0.54
2.80
1.50
0.86
0.45
300
9.7
5.04
3.84
3.29
325
7.5
6.0
4.6
8.1
6.4
4.9
2.74
1.59
0.85
2.08
1.20
0.63
3.16
1.83
0.97
2.40
1.38
0.73
1.77
1.01
0.53
2.04
1.17
0.62
350
8.7
6.9
5.3
3.60
2.08
1.11
2.74
1.58
0.83
2.34
1.34
0.71
375
9.4
7.4
5.7
4.07
2.35
1.25
3.11
1.79
0.95
2.66
1.52
0.80
400
10.0
7.9
6.1
4.56
2.64
1.40
3.50
2.01
1.06
3.00
8.4
6.5
2.94
1.56
2.24
1.18
425
1.72
0.90
1.92
1.01
450
8.9
6.9
3.25
1.73
2.49
1.31
2.13
1.12
475
9.4
7.2
3.58
1.90
2.75
1.45
2.36
1.23
500
9.9
7.6
3.92
2.08
3.02
1.59
2.59
525
8.0
2.27
1.74
1.36
1.48
550
8.4
2.47
1.89
1.62
575
8.8
2.67
2.05
1.76
600
9.1
2.88
2.21
1.90
625
9.5
3.10
2.38
2.05
650
9.9
3.32
2.56
2.20
Flow Velocity above
Shown is pressure
To express
in
– Flow velocity above 8 fps (2.5 m/s) might result in excessive pressurepressure
loss, loss
noise
or erosion of the system components.
considered excessive and
psi per 100 ft
terms of
– Table may
values
in pressure loss units
resultshown
in excessive
of pipe.of psi per 100 ft (30.5 m) of
feetpipe.
of head,
pressure loss, noise or
Example:
for 200 lineal ft of pipe, double the value listed in this table.multiply the value
erosion of system
Example: for 200
listed by 2.307.
– To express
pressure loss in terms of feet
components.
lineal of
ft ofhead,
pipe, multiply the table value by 2.307.
Example: 1 psi =
Example: 1 psi = 2.307 ft of head. double the value
8 feet per second may be
loss in units of
listed in this table.
2.20150309-pressureloss_raupex_rautherm(emailcopyonly) (1).xlsx
18
2.307 ft of head
lee 2163, Page 1 / 1
855.681 en 03.2015
For updates to this publication, visit na.rehau.com/resourcecenter
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using, the user will determine suitability of the information for user’s intended use and shall assume all risk and liability in connection therewith.
© 2015 REHAU
www.rehau.com
[email protected]
855.681 en 03.2015
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