VortexMaster FSV430, FSV450 SwirlMaster FSS430, FSS450 | CI/FSV/FSS/430/450-EN  Rev. G  53 
 
For the energy measurement, the media types "saturated 
steam", "superheated steam" or "hot water“ can be selected. 
 
The calculation is done according to IAPWS-IF97. 
 
Calculation of the net energy for steam 
watersteammp
HHQQ
 
Calculation of the net energy for hot water / condensate 
outwaterinwatermp
HHQQ
__
 
Formula elements used 
Q
 Net energy 
Q
m
 Mass flow 
H
steam
 Steam enthalpy 
H
water
 Water enthalpy 
H
water in
  Water enthalpy (feed flow) 
H
water
out
  Water enthalpy (return flow) 
 
Prerequisites for the energy measurement: 
—  For energy measurement of steam, this must condense 
completely. 
—  The process must form a closed system, energy losses 
through leaks are not recorded. 
 
Steam mass calculation 
The following options are available for the steam mass 
calculation: 
—  Density calculated from the temperature (saturated steam 
only) 
—  Density calculated from the pressure (saturated steam 
only) 
—  Density calculated from pressure and temperature  
— Constant density 
 
If a pressure transmitter is connected, the steam state is 
checked automatically. A distinction is made between wet 
steam, saturated steam, and superheated steam. The correct 
density is always calculated regardless of the selected media 
type. 
 
If a pressure transmitter is not connected and steam type 
"Overheated Steam" is selected, a constant pressure must be 
entered for the state to be detected and, if applicable, the 
density to be calculated. 
 
A value must always be stored for the steam density value 
(constant) in the transmitter in order to define the measuring 
range limits for Q
max
DN in mass flow units. 
An approximation is sufficient here, the density diagrams 
provide an indication for determining the steam density. 
 
Density diagrams 
The following diagrams show an extract from the density table 
for saturated steam at different temperatures / pressures. 
 
Fig. 48:  Saturated steam density vs. temperature 
ρ Steam density  T Temperature 
 
 
Fig. 49:  Saturated steam density vs. pressure 
ρ Steam density  p Pressure 
 
G11882
ρ [kg/m ]³
T
0
2
4
6
8
10
12
14
16
18
20
22
24
26
28
30
32
34
100 115 130 145 160 175 190 205 220 235 250 265 280 [°C]
0
0.1
0.2
0.4
0.5
0.6
0.7
0.9
1.0
1.1
1.2
1.4
1.5
1.6
1.7
1.9
2.0
2.1
212 239 266 293 320 347 374 401 428 455 482 509 536 [°F]
ρ [lb/ft ]³
G11883
ρ [kg/m³]
0
1
2
3
4
5
6
7
8
9
10
11
12
0
0.06
0.12
0.19
0.25
0.31
0.37
0.44
0.50
0.56
0.62
0.69
0.75
024681012141618202224
(0) (29) (58) (87) (116) (145)
(174)
(203) (232) (261) (290) (319)
(348)
p [bar abs (psia)]
ρ [lb/ft³]