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* Production Sizes and Tolerances in accordance with DIN 8077 / December 1997:
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External Diameter dmm
|
Tolerance limit mm
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Wall thickness S mm
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Thickness tolerance mm
|
Approximate unit weight kg/m
|
|
16
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+ 0.3
|
2.7
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+ 0.5
|
0.110
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|
20
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+ 0.3
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3.4
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+ 0.6
|
0.172
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|
25
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+ 0.3
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4.2
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+ 0.7
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0.266
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|
32
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+ 0.3
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5.4
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+ 0.8
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0.434
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|
40
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+ 0.4
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6.7
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+ 0.9
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0.671
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|
50
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+ 0.5
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8.3
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+ 1.1
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1.040
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63
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+ 0.6
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10.5
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+ 1.3
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1.650
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75
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+ 0.7
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12.5
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+ 1.5
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2.340
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90
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+ 0.9
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15.0
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+ 1.7
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3.360
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110
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+ 0.9
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18.3
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+ 2.1
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5.010
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125
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+ 1.2
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20.8
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+ 2.3
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6.470
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* Physical Properties:
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Property
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Test Method
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Unit
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Value
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Density at 23°C
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ISOR 1183
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g/cm3
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0.90
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Melt flow index
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MFI 190°C/5 kg
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ASTM D 1238
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g/10dak.
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0.70
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MFI230°C/2.16kg
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ISOR 1133
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g/I0dak.
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0,2-0,45
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MFI 230°C/5 kg
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DIN 53 735
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g/10dak.
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0,6+1,2
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Fusion point
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°C
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146
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* Thermal Properties:
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Property
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Test Method
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Unit
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Value
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Thermal Conductivity at 23°C
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DIN 52612
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W/m.K
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0.23
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Specific heat at 23°C
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C
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Kj/kg.K
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1.73
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Coefficient of linear
thermal expansion
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DIN 53 752
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K-1
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1. 5-1. 8x1 0-4
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Under weight
deformation temperature 1.8N/mm2
0.45 N/mm2
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ASTM D 648
ISO 75
DIN 53 461
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°C
°C
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44
72
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Breaking temperature
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ASTM D 746
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°C
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-13
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VICAT softening point
(1 kg.)
(5 kg.)
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ASTMD 1525
ISO 306
DIN 53 460
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°C
°C
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130
60
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* Mechanical Properties:
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Properties
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Test Method
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Unit
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Value
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Strength at flow limit at 23°C
Speed of pulling: 50 mm/minute
100 mm/minute
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N/mm2
N/mm2
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22
23
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Extension at flow limit at 23 °C
Speed of pulling: 50 mm/minute
100 mm/minute
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ISO R 527
(Sample No 1)
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%
%
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17
18
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Break strength at 23°C
Speed of pulling: 50 mm/minute
100 mm/minute
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DIN 53455 (Sample No 1)
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N/mm2
N/mm2
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35
34
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Extension of break out at 23°C
Speed of pulling: 50 mm/minute
100 mm/minute
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%
%
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>500
>500
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Elasticity module at 23°C
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ASTM D 790
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N/mm2
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670
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Bend module at 23°C
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DIN 53 447
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N/mm2
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185
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Shore D hardness
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ASTM D 740 ISO R 868,
DIN 53 505
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65
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IZO D impact strength
(notched)at 23°C
at 0°C
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ISO R 180
ASTM D 256
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j/m2
j/m2
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105
30
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CHARPY impact strength
(notched)at 23°C
at 0°C
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DIN 53 453 ISOR 179
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kj/m2
kj/m2
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15
35
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CHARPY impact strength
(unnotched)at 23°C
at 0°C
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DIN 53 453
ISO R 179
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kj/m2
kj/m2
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No break
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Impact strength, at 0°C
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DIN 8078
Part 2
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No break
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* Operating life time in accordance with DIN 8078 / April 1996:
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Temperature
(°C)
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Life
(y)
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Design stress
(MPa)
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20
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50
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9.5
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40
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50
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6.8
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60
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50
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4.7
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70
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50
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3.2
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80
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25
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2.5
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95
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5
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1.85
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* Calculation of Thermal Expansion in PP-R Pipes:
Expansion of the polypropylene pipes are relatively higher and linear expansion coefficient is 11 times bigger than metal pipes. That's why in installations this expansion character must be taken into consideration.
Linear expansion coefficient of ALMATHERM pipes : Temperature is between 30-90°C The expansion DL is calculated through the following formula:
DL =l ´ L ´ DTDL= Linear expansion in mm
lLinear expansion coefficient = mm m.°C
ALMATHERM pipe (Average Value) l0.183 mm m.°C
L = Pipe length in m DT= Temperature difference K or °C
DT= Difference of temperature between hot water and ambience temperature in K or °C
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* Pressure Drops:
Plain pipe pressure loss occurred in 50 meters long pipe used in a normal flat:
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16
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Filling Daiameter
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20
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32
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50
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>063
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25
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40
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63
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Type
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Resistance Coeffiicient
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Elbow 90° curve
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1,5
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1,0
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0,6
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0,5
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Elbow 90° shapr
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2,0
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1,7
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1,1
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0,8
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Elbow 45° curve
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0,3
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Tee
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1,5
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Pipe Entry
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0,5
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Pipe Exit
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1,0
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PS: These Values can be used in calculating the resistance of fittings. For the average value 3-5% must be added to the total pressure loss.
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Pressure drop in the resistances for the loss correction ( x=1 ) ( Dt=10°C and Q=999,7 Kg/m²) being independent from the calculated flow rate (Z=5 ò å x)
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Calculated
flow rate
u
m/s
|
Pressure drop Z
( for x=1 ) mbar
|
Calculated
flow rate
u
m/s
|
Pressure drop Z
( for x=1 )
mbar
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0,1
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0,1
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2,6
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33,8
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0,2
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2,2
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2,7
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36,5
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0,3
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0,5
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2,8
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39,2
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0,4
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0,8
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2,9
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42,1
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0,5
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1,3
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3
|
45
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0,6
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1,8
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3,1
|
48
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0,7
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2,5
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3,2
|
51
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0,8
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3,2
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3,3
|
55
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0,9
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4,1
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3,4
|
58
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1
|
5
|
3,5
|
61
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1,1
|
6,1
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3,6
|
65
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1,2
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7,2
|
3,7
|
68
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1,3
|
8,5
|
3,8
|
72
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1,4
|
9,8
|
3,9
|
76
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1,5
|
11,3
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4
|
80
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|
1,6
|
12,8
|
4,1
|
84
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|
1,7
|
14,5
|
4,2
|
88
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|
1,8
|
16,2
|
4,3
|
92
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|
1,9
|
18,1
|
4,4
|
97
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|
2
|
20
|
4,5
|
101
|
|
2,1
|
22,1
|
4,6
|
106
|
|
2,2
|
24,2
|
4,7
|
110
|
|
2,3
|
26,5
|
4,8
|
115
|
|
2,4
|
28,8
|
4,9
|
120
|
|
2,5
|
31,3
|
5
|
125
|
|
 |
 |
|
The total pressure drop in the pipe (without apparatus resistance) is the result of pressure drop caused by friction in pipes and resistances. Dp = å(L. R + Z)
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 |
|
* Table of Losses
|
 |
|
|
 |
 |
|
|
|
Taps (water source)
|
Debi l/s
|
average flow rate m/s
|
Flow pressure PMF bar
|
ALMATHERM dimension
|
|
Filtered installation Head with filter DN 15 Side filtered head DN 15 Head with filter DN 20 Head with filter DN 25
|
0,15 0,06 0,18 0,31
|
1,41 0,47 1,71 -
|
1,0 1,0 1,0 1,0
|
16 16 16 20
|
|
Bath basins Mixed water valve DN 15 Mixed water valve DN 20 Mixed water valve DN 25
|
0,15 0,4 1,0
|
1,41 1,57 2,36
|
1,0 1,0 1,0
|
16 25 32
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|
Toilets Siphon DN 15 Siphon DN 20 Siphon DN 25 Siphon CaseDN 15
|
0,7 1,0 1,0 0,13
|
1,65 2,36 2,36 1,25
|
1,2 1,2 1,2 0,5
|
32 32 32 16
|
|
Toilet (for urine) Siphon DN 15 Siphon Case DN 15
|
0,3 0,13
|
1,84 1,25
|
1,2 0,5
|
20 16
|
|
Bidet Mixed water valve DN 15
|
0,07
|
0,66
|
1
|
16
|
|
Hospital outlet Mixed water valve DN 15 Siphon DN 20
|
0,12 1,0
|
1,13 2,36
|
1,0 1,2
|
16 32
|
|
Outlets Flow valve DN 15 Mixed water valve DN 15
|
0,12 0,12
|
1,13 1,13
|
1,0 1,0
|
16 16
|
|
Sinks Mixed water valve DN 15 Mixed water valve DN 20
|
0,07 0,02
|
0,66 1,18
|
1,0 1,0
|
16 16
|
|
Sinks Flow valve DN 15 Mixed water valve DN 15
|
0,07 0,07
|
0,66 0,66
|
0,5 1,0
|
16 16
|
|
Flow values without extra flow resistance DN 15 DN 20 DN25 Mixed water valve DN 15 Mixed water valve DN 20
|
0,3 0,5 1,0 0,15 0,30
|
1,84 1,97 2,36 1,41 1,84
|
0,5 0,5 0,5 1,0 1,0
|
20 25 32 16 20
|
|
Dish washing machine Washing machine
|
0,15 0,25
|
1.41 1,53
|
1,0 1,0
|
20 20
|
|
Gas and elektro boiler 6 kw 12 kw 18 kw 21 kw 24 kw 33 kw Elektro thermosiphon DN 15 Low pressure Electro thermosiphon DN 1 5
|
0,07 0,1 0,15 0,17 0,2 0,3 0,15
|
0,66 0,94 1,41 1,61 1,89 1,84 1,41 1,41
|
1,0 1,0 1,0 1,0 1,0 1,0 1,0 0,05
|
16 16 16 16 16 20 16 16
|
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|
 |
|