EB 3132-3 EN
3-7
Design and principle of operation
Table 3-1:
Technical data · Valve
· All pressures in bar (gauge)
Valve size
DN
15
20
25
32
1)
40
1)
50
1)
K
VS
coefficient
Body with
screwed ends
0.4
2)
1.0
2)
2.5
4.0
2)
6.3
8.0
12.5
16.0
20.0
Flanged body
–
12.5
20.0
25.0
x
FZ
value
Body with
screwed ends
0.6
0.55
0.5
0.45
Flanged body
–
0.45
0.4
Pressure rating
PN 25
Max. permissible differential pressure
∆p across the valve
20 bar
16 bar
Max. permissible valve temperature
Liquids 150 °C
Differential pressure set point
Adjusted to 0.2 bar
Conformity
1)
Additional version: valve with flanged body made of spheroidal graphite iron (EN-GJS-400-18-LT)
2)
Special version
Table 3-2:
Flow rate set point ranges
Flow rate set point ranges
V
for water in m³/h
Δp
set point
Δp
plant
+ Δp
restriction
Δp
plant
Calculation
for plant
Δp
restriction
Differential
pressure
across the
restriction
DN
15
20
25
32
40
50
K
VS
0.4
1)
1.0
1)
2.5 4.0
1)
6.3
8.0 12.5 16.0 20.0
V
min.
0.01 0.12 0.2
0.5
0.8
0.8
2
3
4
0.2 bar
0.1 bar
0.1 bar
V
max.
0.14 0.45 0.85 1.8
2.6
3.6
7.1
8.5 10.7
0.3 bar
0.1 bar
0.2 bar
V
max.
0.2 0.64 1.2
2.5
3.6
4.2 10.0 12.5 15.0
–
1.3
2)
2.3
2)
3.5
2)
5.8
2)
9.1
2)
14.1
2)
1)
Special version
2)
An increase in noise level can be expected when the specified flow rate is exceeded, even if cavita
-
tion does not occur (see AGFW (German District Heating Association) document FW 514).
See Fig. 3-3 to calculate the minimum required differential pressure
Δpmin
between the
flow
pipe and return flow pipe
.
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