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1.12. DADOS ESTUFAS.
MARSELLA
RS
PARÍS
RP
BOLONIA
VPA 00-00
TOKIO
CO 00-00
LIGAÇÕES

Extractor saída gases Ø
mm
80
80
80
80

Tubo entrada ar estanque Ø
mm
30
30
- -
- -

Canalização ar convecção Ø
mm
- -
- -
1x100
- -
ADMISSÃO AR
Volume ar admissão máximo*
m3/h
36,2
41,0
43,2
46,2
Tiragem mínima recomendada
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
CARACTERÍSTICAS GERAIS
Peso
Kg
115
110
143
146
Combustível de pellets de madeira.
A1
Si
Si
Si
Si
Capacidade da depósito**
Kg
15
20
20
30
Termóstato de segurança tarado
°C
125
125
93
93
Sonoridade a nível 9, 3m de distância e 1,5m de altura
dB
42,5
42,5
44,1
48,1
POTÊNCIA TÉRMICA NOMINAL
Queda máxima de combustível
1 - 9
9
9
9
9
Potência térmica reduzida
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 aproximada
h
9
9
9
11
Conteúdo CO (al 13% de 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
Caudal mássico de fumos
g/s
8
9
10
10
Tª média de fumos
°C
170
173
173
180
Consumo de energia auxiliar
W
180
80
90
255
Fluxo e temperatura média do ar canalizado.
m3/h
- -
- -
- -
°C
- -
- -
- -
POTÊNCIA TÉRMICA REDUZIDA
Queda máxima de combustível
1 - 9
1
1
1
1
Potência térmica reduzida
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 aproximada
h
15
26
19
27
Conteúdo CO (al 13% de 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
Caudal mássico de fumos
g/s
5
7
5
8
Tª média de fumos
°C
70
100
95
110
Consumo de energia auxiliar
W
88
44
30
130
Eficiência energética sazonal de aquecimento
ambiente (ŋs).
%
85,2
83,7
86,8
84,6
* Estimativa dependendo do fluxo de massa e temperatura do gás no nominal
**Estimativa combustível
ρap≈630 kg/m3
UNE EN 14785
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