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Nibe FIGHTER 1330 - Pressure Expansion Vessel; Limiting Condenser out and Condenser in; Available Pressure, Heating Medium Side; Available Pressure, Brine Side (Ethanol 28 %)

Nibe FIGHTER 1330
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0
0
mvp kPa
500
1000
1500
0
l/h
2000
2
4
8
20
80
40
Tryck
Flöde
1
2
3
2500 3000 3500 5000 4500 4000
60
6
FIGHTER 1320-20
100
10
1
2
3
0
0
mvp kPa
500
1000
1500
0
l/h
2000
2
4
8
20
80
40
Tryck
2500 3000 3500 5000 5500 6000 4500 4000
60
6
FIGHTER 1320-25/30/40
Flöde
100
10
0
1000
2000
l/h
3000
Tryck
4000 5000 6000 80007000
FIGHTER 1330-22/30/40
Flöde
0
0
5
10
20
50
200
100
150
15
250
25
mvpkPa
300
30
22
30
40
Pipe connections
11
FIGHTER 1330
Available pressure, collector side (ethanol 28 %)
Available pressure, heating medium side
The brine circuit should be fitted with a pressure
expansion
vessel. If there is a level vessel, this should
be replaced. The brine
side should be pressu rised to
at least 0.5 bar.
The pressure expansion vessel should be dimen-
sioned as set out in the diagram, to prevent operat-
ing disturbances. The pressure expansion vessel cov-
ers the temperature range from -10 °C to +20 °C at a
pre-pressure of 0.5 bar and the safety valve’s opening
pressure 3 bar.
Pressure expansion vessel
l
l
Pressure expansion vessel
Brine
volume
30
0
40
50
60
0
10
20
100 200 300 400 500 600 700 800 900 1000 1100 1200 1300 1400 1500
FIGHTER 1330 -22
FIGHTER 1330 -22/30/40
FIGHTER 1330-30/40
Pressure
Pressure
Pressure
Flow
Flow
Flow
For HTF in hotter than -5 °C, limiting of max conden-
ser out 65 °C and max condenser in 58 °C.
For HTF in colder than -5 °C, max condenser out and
max condenser in lowers automatically, according to
diagram, additional heat maintains desired supply
temperature.
For HTF in lower than -8 °C, the compressor stops and
the desired supply temperature is only maintained by
additional heat.
50
52
54
56
58
60
62
64
66
68
70
-9 -7 -5 -3 -1 1 3 5 7 9 11 13 15 17 19 21
1
2
°C
°C
Köldbä-
rare in
Kondensor ut
Limiting condenser out and
condenser in
1. Condenser out 2. Condenser in
Condenser out
Brine
in

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