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1.12. DATI DELLE STUFE.
MARSELLA
RS
PARÍS
RP
BOLONIA
VPA 00-00
TOKIO
CO 00-00
COLLEGAMENTI

Estrattore della fuoriuscita di gas Ø
mm
80
80
80
80

Tubo di ingresso dell'aria stagno Ø
mm
30
30
- -
- -

Canalizzazione dell'aria di convezione Ø
mm
- -
- -
1x100
- -
AMMISSIONE D'ARIA
Flusso d'aria di aspirazione massimo*
m3/h
36,2
41,0
43,2
46,2
Tiraggio minimo consigliato
mBar
0,10 0,12
0,10 0,12
0,10 0,12
0,10 0,20
Pa
10 - 12
10 - 12
10 - 12
10 - 20
CARATTERISTICHE TECNICHE
Peso
Kg
115
110
143
146
Combustibile per pellet di legno.
A1
Si
Si
Si
Si
Capacità del serbatoio**
Kg
15
20
20
30
Termostato di sicurezza tarato
°C
125
125
93
93
Livello sonoro a 9, 3m di distanza e 1,5m di altezza
dB
42,5
42,5
44,1
48,1
POTENZA TERMICA NOMINALE
Livello di caduta di combustibile
1 - 9
9
9
9
9
Potenza termica nominale
kW
9,9
10,0
10,0
12,0
Rendimento
%
90,0
87,0
90,0
90,0
Consumo
kg/h
2,2
2,3
2,2
2,7
Autonomia approssimativa
h
9
9
9
11
Contenuto CO (al 13% di O2)
%
0,02
0,01
0,02
0,02
mg/Nm3
240
101
241
239
NOx.
mg/Nm3
188
185
196
190
OGC.
mg/Nm3
6
12
17
18
PM.
mg/Nm3
19
18
20
19
Portata massica dei fumi
g/s
8
9
10
10
Tª media dei fumi
°C
170
173
173
180
Consumo di energia elettrica ausiliaria
W
180
80
90
255
Flusso e temperatura media dell’aria canalizzata.
m3/h
- -
- -
- -
°C
- -
- -
- -
POTENZA TERMICA RIDOTTA
Livello di caduta di combustibile
1 - 9
1
1
1
1
Potenza termica ridotta
kW
4,5
3,2
4,9
5,0
Rendimento
%
92,0
84,0
92,9
91,0
Consumo
kg/h
1,0
0,8
1,0
1,1
Autonomia approssimativa
h
15
26
19
27
Contenuto CO (al 13% di O2)
%
0,02
0,02
0,02
0,02
mg/Nm3
285
288
297
243
NOx.
mg/Nm3
196
189
194
195
OGC.
mg/Nm3
10
29
19
19
PM.
mg/Nm3
20
19
20
20
Portata massica dei fumi
g/s
5
7
5
8
Tª media dei fumi
°C
70
100
95
110
Consumo di energia elettrica ausiliaria
W
88
44
30
130
Eficienza energética stagionale del riscaldamento
d’ambienti (ŋs).
%
86,8
86,8
86,8
84,6
* Stima secondo flusso di massa e temperatura del gas a potenza nominale
**Stima combustibile
UNE EN 14785
109


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