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280
300
330
360
Heat capacity recovered
kW
282
316
345
375
Desuperheater water flow rate
l/h
48430 54340 59420 64500
Desuperheater pressure drops
kPa
20.8
28.3
30.3
38.5
15. DESUPERHEATER
The heating capacity that can be
obtained from the desuperheater is
obtained by multiplying the nominal
value (Pd) shown in table 15.1.1 by a
suitable coefficient (Cd).
The diagrams will give you the correction
coefficients to be used for the chillers in
the various versions; next to each curve
you can see the outside air temperature
to which it refers.
In the heat pump versions, the
desuperheater must be intercepted
during heat pump operation: otherwise,
the guarantee will no longer be
considered valid.
15.1. PRESSURE
DROPS
The NRL models with desuperheater, from
size 2800 to 3600, have 4 desuperheaters
(placed in parallel 2 to 2).
NB:
the characteristics of the desuperheaters
and the pressure drop curves are shown
below.
For processed water temperatures
different from 50°C, the result obtained
is multiplied by the correction factor that
can be obtained from Table 15.1.2.
Processed water temperature at the desuperheater (
∆
t 5°C)
Cd correction coefficient
45°C
40°C
35°C
30°C
25°C
0.00
35
40
45
50
55
60
65
0.50
1.00
1.50
2.00
2.50
3.00
20°C
DESUPERHEATER CORRECTION COEFFICIENTS
0
20
40
60
80
100
120
140
160
180
200
20000
30000
40000
50000
60000
70000
80000
90000
100000
110000
120000
Portata acqua [l/h]
P
e
rd
it
a
d
i c
a
ri
c
o
to
ta
le
[k
P
a
]
2800
3000
330
0
36
00
DESUPERHEATER PRESSURE DROPS
NOTES:
The units with desuperheater (D)
not for versions:
−
YD
−
XD (only for temperatures lower than 4°C)
Average water temperature °C
30
40
50
60
70
Multiplication coefficient
1.04
1.02
1
0.98
0.96
The nominal value refers to:
−
air temperature
35°C
−
water at the desuperheate 45/50°C
−
∆
t 5°C
15.1.1. NRL (D)
15.1.2. Correction of pressure drop when
average water temperature varies.
27
INRLPY. 02.10 4086916_01
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