13
Technical characteristics and dimensions
2.4 OPERATING DATA AND GENERAL CHARACTERISTICS
ARES Tec ErP 150 200 250 300 350
Boiler category II
2H3P
II
2H3P
II
2H3P
II
2H3P
II
2H3P
Modulation ratio 1 : 12,5 1 : 16,7 1 : 20,8 1 : 25 1 : 29
Nominal heat input on L.V.C. Qn kW 150 200 250 300 348
Minimum heat input on L.C.V. Qmin kW 12 12 12 12 12
Nominal eective power (Tr 60 / Tf 80 °C) Pn kW 146,1 195,2 244,5 294,0 341,7
Minimum eective power (Tr 60 / Tf 80 °C) Pn min kW 11,7 11,7 11,7 11,7 11,7
Nominal eective power (Tr 30 / Tf 50 °C) Pcond kW 150 200,4 251,3 302,7 354,6
Minimum eective power (Tr 30 / Tf 50 °C) Pcond min
kW 12,8 12,8 12,8 12,8 12,8
Eciency at nominal power (Tr 60 / Tf 80°C) % 97,4 97,6 97,8 98,0 98,2
Eciency at minimum power (Tr 60 / Tf 80°C) % 97,16 97,16 97,16 97,16 97,16
Eciency at nominal power (Tr 30 / Tm 50°C) % 100,0 100,2 100,5 100,9 101,9
Eciency at minimum power (Tr 30 / Tm 50°C) % 106,5 106,5 106,5 106,5 106,5
Eciency at 30% of the load ( Tr 30°C) % 107,3 107,3 107,3 107,3 107,3
Eciency class according to directive 92/42 EEC -- 4 4 4 4 4
Combustion eciency at nominal load % 97,8 97,8 98,0 98,1 98,3
Combustion eciency at a reduced load % 98,3 98,3 98,3 98,3 98,3
Losses from operating burner casing (Qmin) % 1,2 1,2 1,2 1,2 1,2
Losses from operating burner casing (Qn) % 0,4 0,2 0,2 0,1
0,1
Flue temperature at net of Tf-Ta (min)(*) °C 33,4 33,4 33,4 33,4 33,4
Flue temperature at net of Tf-Ta (max)(*) °C 45,1 46,5 47,3 48,2 49,1
Maximum permitted temperature °C 100 100 100 100 100
Maximum operating temperature: °C 85 85 85 85 85
Mass ue ow rate (min) kg/h 19,6 19,6 19,6 19,6 19,6
Mass ue ow rate (max) kg/h 245 327 409 490 569
Air excess % 25,5 25,5 25,5 25,5 25,5
Chimney losses with burner in operation (min) % 1,7 1,7 1,7 1,7 1,7
Flue losses with burner in operation (max) % 2,2 2,2
2,2 1,9 1,7
Minimum pressure of h
eating circuit bar 0,5 0,5 0,5 0,5 0,5
Maximum pressure of heating circuit bar 6,0 6,0 6,0 6,0 6,0
Water content l 14,2 18,3 22,4 26,5 30,6
Methane gas consumption G20 (supp.press. 20 mbar) at Qn m
3
/h 15,9 21,1 26,4 31,7 36,8
Methane gas consumption G20 (supp.press. 20 mbar) at Qn m
3
/h 1,3 1,3 1,3 1,3 1,3
Gas consumption G25 (supp.press. 20/25 mbar) at Qn m
3
/h 18,4 24,6 36,7 36,9 42,8
Gas consumption G25 (supp.press. 20/25 mbar) at Qn m
3
/h 1,5 1,5 1,5 1,5 1,5
Propane gas consumption (supp.press. 37/50 mbar) at Qn kg/h 11,6 15,5 19,4 23,3 27
Propane gas consumption (supp.press. 37/50 mbar) at Qn kg/h 0,9 0,9 0,9 0,9
0,9
Maximum pressure available at ue base Pa 100 100 100 100 100
Max condensate production kg/h 23
30,60 38,3 45,9 53,6
Emissions
CO at maximum heat input with 0% O2 mg/kWh
54
62 71 55 58
NOx at maximum hea
t input with 0% O2 mg/kWh
38 36 44 42 40
NOx class 6 6 6 6 6
(***) So
und pressure level dBA 52 52 52 52 52
Electrical data
Frequency/Power supply voltage: V/Hz 230/50 230/50 230/50 230/50 230/50
Supply fuse A (R) 6,3/10 6,3/10 6,3/10 6,3/10 6,3/10
(**) Degree of protection IP X5D X5D X5D X5D X5D
For the adjustment data: NOZZLES - PRESSURES - DIAPHRAGMS - FLOW RATES refer to the paragraph ADAPTATION FOR USE WITH OTHER GASES.
Room Temperature = 20°C
(*) Temperatures read with the device operating with ow 80°C / ret. 60°C
CO
2
(min/max) See “NOZZLES - PRESSURES” table
Seasonal Energy Eciency according to 2009/125 EEC (<=400Kw) η
s
- see Table ErP
Losses at shutdown at ∆T 30°C - Pstb - see Table ErP
Electrical consumption in standby - Psb - see Table ErP
(**) e IP X5D degree of protection is obtained with the lid lowered
(***) at a distance of 1 m in a free eld.