21
Ethylene glycol solution
-30
-25
-20
-15
-10
-5
0
5
0 5 10 15 20 25 30 35 40 45 50
-35
0,99
0,98
0,97
0,96
0,95
1,00
1,10
1,20
1,30
1,40
1,50
1,60
1,70
1,80
1,90
2,00
2,10
-35
55
-40
0,94
2,20
FcGPf
FcGPa
FcGPf (PdC)
FcGQPdc
FcGQF
FcGDpF (d)
FcGDpF (c)
FcGDpF (b)
FcGDpF (a)
FcGDpF (e)
Fattore correttivo
Temperatura aria esterna
(°C)
% GLICOLE
Temperatura
acqua prodotta (°C)
5
-6
(1)
0
Key::
FcGPf =
Correction factor
of the cooling
capacity
FcGPa =
Input power
correction factor.
FcGDpF (a) =(Evaporator) pressure drop
correction factor (evaluated with an
average temperature of -3.5 °C)
FcGDpF (b) = Correction factor of the
pressure drops (average temperature =
0.5 °C)
FcGDpF (c) = Correction factor of the
pressure drops (average temperature =
5.5 °C)
FcGDpF (d) = Correction factor of the
pressure drops (average temperature =
9.5 °C)
FcGDpF (e) =
Correction factor of the
pressure drops (average temperature =
47.5 °C)
FcGQF =Flow rate (evap) correction
factor mean temperature
=
9.5 °C)
FcGQC =Flow rate (condenser) correction
factor mean temperature
=
47.5 °C)
The water flow rate and pressure drop
correction factors must be applied
directly to the data obtained for operation
without glycole.
fig. 03