1.3
TECHNICAL FEATURES
Heat output
Nominal
Minimum
D.H.W. heat output
Nominal
Heat input
Nominal
Minimum
Water content
Adsorbed power consumption
Electrical protection grade
Maximum water head
Maximum temperature
Expansion vessel
Water content/Preloading pressure
C.H. setting range
D.H.W. setting range
D.H.W. production
Tank capacity
Continuous D.H.W. flow rate at ∆t 30°C
Specific D.H.W. flow rate EN 625
D.H.W. maximum water head
Recovery time from 25°C to 55°C
D.H.W. expansion vessel
Smoke temperature
Smoke flow
Category
Type
Weight
Main gas nozzles
Quantity
Methane
G30 - G31
(2)
Gas flow
Methane
Butane (G30)
Propane (G31)
Gas burner pressure
Methane
Butane (G30)
Propane (G31)
Gas supply pressure
Methane
Butane (G30)
Propane (G31)
(1) Flow calculated with a fixed temperature on the D.H.W. potentiometer of 60 °C for a maximum period of 10 minutes
(2) The gas consumptions refers to the calorific value at standard conditions at 15°C - 1013 mbar
(3) Differential measure between the pressure upstream of the gas valve and the depression in the sealed room
74
kW
kcal/h
kW
kcal/h
kW
kW
kW
l
W
bar
°C
l/bar
°C
°C
l
l/h
(1)
l/min
bar
min
l
°C
gr/s
kg
n°
ø mm
ø mm
m
3
st/h
kg/h
kg/h
mbar
mbar
mbar
mbar
mbar
mbar
25/60 OF
25/60 BF
8,4 ÷ 23,2
9,3 ÷ 25,0
7.200 ÷ 20.000
8.000 ÷ 21.500
8,4
7.200
8.000
23,2
10,8 ÷ 25,8
10,8 ÷ 26,7
10,8
4
105
IP X4D
IP X4D
3
85
8/1
40÷80
40÷80
10÷60
10÷60
60
684
14,5
7
4' 30"
4' 30"
2,5
110
21,0
II
2H3+
B
C
- C
11BS
12
74
13
1,30
0,75
2,73
1,99
1,96
1,8÷9,7
1,9÷ 10,8
4,7÷27,4
4,7÷28,4
6,3÷35,3
4,7÷35,3
20
30
37
30/60 BF
11,6 ÷ 29,5
10.000 ÷ 25.400
9,3
11,6
10.000
25,0
29,5
13,5 ÷ 31,6
10,8
13,5
4
5
165
180
IP X4D
3
3
85
85
8/1
8/1
40÷80
10÷60
60
60
684
774
14,5
16, 1
7
7
4'
2,5
2,5
123
123
17,0
20,0
II
II
2H3+
2H3+
- C
- C
C
- C
- C
32
42
52
12
32
42
82
82
13
15
1,30
1,30
0,76
0,76
2,83
3,34
2,06
2,44
2,03
2,40
(3)
1,7÷ 11,3
(3)
4,7÷28, 1
(3)
4,7÷35,9
20
20
30
30
37
37
- C
52
(3)
(3)
(3)