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1. SPÉCIFICATIONS TECHNIQUES.
HIDROCOPPER 18
HIDROCOPPER 24
HV 00-03
SLIM
HP 00-02
SLIM+
HQ 00-01
HW 00-01
SLIM
HX 00-01
CONNEXIONS
Retour du circuit chauffage -
femelle
3/4 3/4
Départ du circuit chauffage:
femelle
1/2 1/2
Charge du circuit femelle
3/4
3/4
Soupape de sécurité femelle
1/2
1/2
Évacuation des gaz
mm
100
100
Entrée d'air
mm
60
60
APPORT D’AIR
Flux d'apport d’air maximale *
m3/h
202,8
237,4
Tirage minimal recommandé
mBar / Pa
10
10
HYDRAULIQUE
Vase d’expansion
8 L | -10/+100 °C
0,75 Bar | 3 Bar máx
Pression de service maximale
Bar / KPa
2,2 / 220
Pression de service minimale
Bar / KPa
0,8 / 80
Pression de service conseillée
Bar / KPa
1,2 / 120
Soupape de sécurité
Bar / KPa
3 / 300
Volume eau intérieur chaudière
L
CARACTÉRISTIQUES GÉNÉRALES
Poids
Kg
133
154
162
171
--
Capacité de la trémie **
Kg
23
36
36
32
40
Sonorité à un niveau de distance de 9, 3m et
1,5m de haut
dB 46 46
PUISSANCE THERMIQUE NOMINALE
Niveau de la chute de carburant
1 - 9
9
9
Puissance thermique nominale
kW
18
23,6
Rendement
%
93
92
Consommation
kg/h
3,9
5,1
Autonomie approximative
H
6
6
9
6
8
Teneur en CO (à 13% d’O
2
)
%
0,02
0,02
Débit massique des fumées
g/s
47
55
Tº moyenne des fumées
°C
150
150
Consommation d'énergie auxiliaire
W
120
48
PUISSANCE THERMIQUE REDUITE
Niveau de la chute de carburant
1 - 9
1
1
Puissance thermique reduite
kW
9,5
9,5
Rendement
%
95
94
Consommation
kg/h
2
2
Autonomie approximative
H
12
16
16
16
20
Teneur en CO (à 13% d’O
2
)
%
0,02
0,02
Débit massique des fumées
g/s
31
28
Tº moyenne des fumées
°C
70
90
Consommation d'énergie auxiliaire
W
35
26
* Estimation selon le débit massique et la température du gaz au nominal.
**Estimation combustible. ρap≈630 kg/m3
52


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