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Pressure Pipe System Rating
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72. Pressure pipe systems ratings
Thermoplastic pipes based on the nominated standard sizes
are accorded pressure ratings. The basis of this rating is that
the outside diameter of the pipe remains standard but the
wall thickness is specifi ed according to the strength
requirement. For example the outside diameter of a 32 mm
pressure pipe rated at 10 bar will be the same as that rated
at 16 bar. The higher the pressure that the pipe is required to
hold, the greater the strength requirement and thus the
greater the wall thickness necessary to withstand that
pressure.
2.1 Calculation of pipe wall thicknessThe pipe wall thickness can be calculated by the following
vessel formula:-
2.2 International standards of ratings
There are three classifi cations which are accepted as
International Standards for rating of plastic pipes: -
2.2.1 The PN Nominal Pressure classifi cationThe PN classifi cation rates pipes and components for their
maximum permissible pressure at 20C. Thus a component
rated at PN16 can be used to carry liquid or other fl uid
media at 20C up to a maximum pressure of 16 bar.
This system also rules that pipes, valves and fi ttings of the
same standard size and same nominal pressure rating will
have the same joint dimensions.
2.2.2 The ISO 4065 S series classifi cationThe ISO 4065 S classifi es pipes into pressure ratings using a
series number, therefore pipes with the same series number
are rated to the same pressure.
The series number can be arrived at by use of the
following formula: -
Where e Pipe wall thickness (mm) D Outside diameter (mm) P Permissible operating pressure (bar) at 20 C Permissible circumferential stress (MPa),
HPPE=10 MPa.
20 Constant of proportionality
Due to manufacturing necessity pipes of a small diameter will
have a greater wall thickness than may be expected when
using the vessel formula.
Where S Series number, note this is dimensionless Permissible circumferential stress (MPa),
HPPE=10 MPa.
P Permissible operating pressure (bar) at 20 C 10 Proportionality constant
D Outside diameter (mm) e Pipe wall thickness (mm)
2.2.3 The SDR (Standard Dimension Ratio)The SDR rating (an American classifi cation) denotes the ratio of
the pipes outside diameter to its wall thickness and is found
by using: -
Where SDR Standard Dimension Ratio D Outside diameter (mm) e Pipe wall thickness (mm), this may be calculated using the vessel formula
The SDR may also be calculated from the ISO 4065 S Series (S) by use of the following formula: SDR = 2 x S + 1
Alternatively S can be derived with
Table 2.1 Correlation between SDR and PN
PE100 - Safety Factor S = 1.25
SDR PN
33 5
26 6.3
21 8
17 10
11 16
7.4 25
PN is valid for 20C water for service life of 50 years
Pressure Pipe System Ratings
1
8The required duration of operation for a given working
pressure and temperature must be taken into account when
planning a plastic pipe system. Pressures that can be
sustained for a short time at a certain temperature may not
be sustainable at a higher working temperature; or even at
the same pressure and temperature should the working
duration of the system be extended. It is possible to work
out the maximum permitted working pressures at different
temperatures and the associated safety factors with the
use of regression graphs. Safety factors are used to ensure
that plastic pipeline systems can operate under stress for their
given lifetime without damage or failure and is described as
the ratio between the maximum allowable circumferential
stress which a system can absorb and its operating stress.
Where P Permissible operating pressure (bar) C Safety factor (see table 3.1) 20 Proportionality constant Circumferential stress (MPa), taken from
regression chart (see chart 3.1).
e Pipes wall thickness (mm) D Pipes outside diameter (mm)
Note that fi ttings and other components, with the same
pressure rating as the pipe, are normally thicker walled and
therefore the lowest common denominator of wall thickness
(e) should be used.
Table 3.1 Safety factors for thermoplastics (C)
Thermoplastic material
HPPE PVCu metric PVCu imperial ABS metric ABS imperial
Safety factor* 1.25 2.5 2.1 2.1 2.1
3. Pressure and temperature relationship The following formula is used to calculate the permissible working pressure for a pipeline system: -
* Safety factors are based on 50 year expected life at 20C, with water.
The higher the working temperature of a plastic pipe system, the lower will be the working pressure that can be sustained
within the system, please refer to table 3.2.
(PN10) for 3.8 mm wall thickness
and
(PN10) for 3.8 mm wall thickness
and
(PN16) for 5.8 mm wall thickness (PN16) for 5.8 mm wall thickness
Worked example 3.1Calculate the maximum operating pressure for a pipe system
with the following specifi cation:-
Material type: HPPE
Intended operating life: 5 years
Maximum operating temperature: 20 C
Pipe dimensions: 63 x 3.8 mm and 63 x 5.8 mm
SolutionFactor of safety C = 1.25 (from table 3.1).With life span 5 years and temperature t = 20 C fi nd = 10.4
(from chart 3.1).
The formula for determining the operating pressure is used:-
Worked example 3.2Calculate the maximum operating pressure for a pipe system
with the following specifi cation:-
Material type: HPPE
Intended operating life: 25 years
Maximum operating temperature: 30 C
Pipe dimensions: 63 x 3.8 mm and 63 x 5.8 mm
SolutionFactor of safety C = 1.25 (from table 3.1).With life span 25 years and temperature t = 30 C fi nd = 8.5
(from chart 3.1).
The formula for determining the operating pressure is used: -
20 10.4 3.81.25 (63 3.8)
10.7 bar3.8
20 8.5 3.81.25 (63 3.8)
8.7 bar3.8
20 8.5 5.81.25 (63 5.8)
13.8 bar5.8
20 10.4 5.81.25 (63 5.8)
16.9 bar5.8
Pressure andTemperature Relationship
2
9Tab
le 3
.2 P
ress
ure
/tem
per
atu
re r
elat
ion
sip
Ter
rain
HPP
E p
ress
ure
(sa
fety
fac
tor
1.25
)
Temperature C
Operating years
S cl
asifi
cat
ion
2520
1612
.510
.510
8.3
86.
35
43.
22.
52
SDR
cla
ssifi
cat
ion
5141
3326
2221
17.6
1713
.611
97.
46
5
PN r
atin
g
105
4.0
5.0
6.3
7.9
9.4
10.1
12.1
12.6
15.7
20.2
25.2
31.5
40.4
50.5
103.
94.
96.
27.
89.
39.
911
.912
.415
.519
.824
.831
.039
.749
.6
253.
84.
86.
07.
69.
09.
611
.612
.115
.119
.324
.230
.238
.748
.4
503.
84.
75.
97.
58.
99.
511
.411
.914
.819
.023
.829
.738
.047
.6
100
3.7
4.6
5.8
7.3
8.7
9.3
11.2
11.6
14.6
18.7
23.3
29.2
37.4
46.7
205
3.3
4.2
5.3
6.6
7.9
8.4
10.2
10.6
13.2
16.9
21.2
26.5
33.9
42.4
103.
34.
15.
26.
57.
88.
310
.010
.413
.016
.620
.826
.033
.341
.6
253.
24.
05.
06.
47.
68.
19.
810
.112
.716
.220
.325
.432
.540
.7
503.
24.
05.
06.
37.
58.
09.
610
.012
.516
.020
.025
.032
.040
.0
100
3.1
3.9
4.9
6.1
7.3
7.8
9.4
9.8
12.2
15.7
19.6
24.5
31.4
39.2
305
2.8
3.6
4.5
5.6
6.7
7.2
8.6
9.0
11.2
14.4
18.0
22.5
28.8
36.0
102.
83.
54.
45.
56.
67.
08.
58.
811
.014
.117
.722
.128
.335
.4
252.
73.
44.
35.
46.
46.
98.
38.
610
.813
.817
.221
.627
.634
.5
502.
73.
34.
25.
36.
36.
78.
18.
410
.613
.516
.921
.227
.133
.9
405
2.4
3.0
3.8
4.8
5.8
6.1
7.4
7.7
9.6
12.3
15.4
19.3
24.7
30.9
102.
43.
03.
84.
75.
76.
07.
37.
69.
512
.115
.219
.024
.330
.4
252.
32.
93.
74.
65.
55.
97.
17.
49.
211
.814
.818
.523
.729
.7
502.
32.
93.
64.
55.
45.
87.
07.
29.
111
.614
.518
.223
.329
.1
505
2.1
2.6
3.3
4.2
5.0
5.3
6.4
6.7
8.3
10.7
13.4
16.7
21.4
26.8
102.
02.
63.
24.
04.
85.
26.
26.
58.
110
.413
.016
.220
.326
.0
151.
92.
32.
93.
74.
44.
75.
75.
97.
49.
511
.814
.819
.023
.7
605
1.5
1.9
2.4
3.0
3.6
3.8
4.6
4.8
6.0
7.7
9.7
12.1
15.5
19.4
702
1.2
1.5
1.9
2.4
2.9
3.1
3.7
3.9
4.9
6.2
7.8
9.8
12.5
15.7
Op
erat
ing
Ye
ars
Tem
pera
ture
C
3
10
25
20
1
10
1.5
0.5
1
2
2.5
3
3.5
4
5
6
7
8
9
10
100 1000 10000 100000 100000 10000000Time (h)
Years
Circ
umfe
rent
ial S
tres
s (M
Pa)
15
1005025101 5
20C
30C
40C
50C
60C
10C
Chart 3.1 Life Regression for HPPE
Pressure andTemperature Relationship
4
11
It is recommended that if the allowable negative pressure
(Pe) is less than 1 bar then the pipeline system will not sustain vacuum. (1 bar = 0.98 Atmospheres.) Different thermoplastics
have different operating temperatures under a vacuum and
maximum installation temperatures must be observed, as
shown in table 3.3: -
Worked example 3.3A HPPE pipe operates under the following condition: -
Pipe outside diameter: 110mm
Intended service life: 10 years
Safety factor: 2
Modulus of Elasticity 900 MPa
Poissons Ratio 0.4
Determine the collapsing pressure and determine whether the
vacuum pressure can or can not be sustained,
for two cases: -
Pipe wall thickness: 6.6mm
Pipe wall thickness: 3.4mm
SolutionThe collapsing pressure is given by: -
(a) For e = 6.6mm, the collapsing and the vacuum pressure are calculated: -
Therefore the pipe will sustain this condition,
as Pe is greater than 1.
(b) For e = 3.4mm, the collapsing and the vacuum pressure are calculated: -
This pressure is lower than 1 bar; hence the pipe system can
not support this condition.
3.1 Maximum working conditions for
negative pressure
The design safety factor for negative
pressure is 2.
Pipeline systems operating below atmospheric pressure
(1 bar) are subjected to vacuum or negative pressure
and will tend to collapse radially inwards due to the
greater outside pressure.
The collapsing pressure can be shown by the following
formula: -
Where Pc Collapsing pressure (bar) 20 Proportionality constant
E Modulus of elasticity (MPa) (See table 1.1) Poissons ratio (0.4 for plastic) e Pipe wall thickness (mm) D Pipe outside diameter (mm) C Safety factor = 2 (Design safety factor for negative pressure)
The maximum allowable negative pressure (Pe) is obtained from the collapsing pressure (Pc) and safetyfactor (C) with: -
Table 3.3 Maximum installation temperatures for vacuum conditions
Thermoplastic material Maximum temperature under vacuum (C)
PN10 PN16
PE 60 60
PVCu 40 60
ABS 60 60
PP 80 80
20 900 (6.6/110)3 4.63 bar
2.31 bar4.63
20 900 (3.4/110)3 0.63 bar
0.63 0.32
5