SMART BOILERS OPERATING DATA |
Marking |
|
350 |
Nominal power Pn |
kW |
350 |
Partial load (power) Pp |
kW |
90 |
Boiler efficiency at Pn |
% |
>95 |
Boiler class |
|
5 |
Water volume |
l |
740 |
Diameter of water connection |
“ |
4 |
Diameter of water connection |
DN |
100 |
Hydraulic-pressure drop of the boiler at the temperature fall 20° |
mbar
|
102
|
Boiler temperature |
°C |
60–90° |
Minimal temperature of returnable water |
°C |
55 |
Maximal operational pressure |
bar |
3,5 |
Test pressure |
bar |
6,5 |
Temperature of furnace |
°C |
900–1100 |
Pressure of furmace |
mbar |
-0,04 |
Required draught of the chimney |
mbar |
0,2 |
Requirement for the forced draught |
|
Yes |
Combustion temperature at Pn |
°C |
99,3 |
Combustion temperature at Pp |
°C |
62,1 |
Diameter of flue gas duct |
mm |
300 |
Diameter of chimney |
mm |
350 |
Wood pellets – C1 |
Tested fuel |
D6, M10, A1,5, DU90,0 |
Wood chips – B1 |
P45, M30, A3.0 |
Electrical connection |
|
3+N+PE 50Hz 230/400V TN-C-S |
Conveyor engine |
W |
550 |
Feeding auger engine |
W |
550 |
Exchanger cleaning engine (s) |
W |
2 x 550 |
Ash-removing engine |
W |
550 |
Fan of primary air |
W |
66 |
Fan of secondary air 1 |
W |
170 |
Fan of secondary air 2 |
W |
170 |
Chimney exhaust fan |
W |
1100 |
Electrical ignition |
W |
1600 |
Separation flap valve |
W |
6,5 |
|
Wood pellets |
Wood chips |
Rated |
Minimum |
Rated |
Minimum |
Rated heat capacity |
kW |
350 |
350 |
350 |
350 |
Combustion producttemperature |
°C |
93,8 |
63,1 |
99,3 |
62,9 |
Fuel consumption |
kg/hour |
78,90 |
18,50 |
86,90 |
20,80 |
Input water temperature |
°C |
58,4 |
60,6 |
59,3 |
57,7 |
Outlet water temperature |
°C |
75,5 |
76,1 |
75,0 |
74,5 |
Cooling water temperature |
°C |
9,5 |
10,7 |
9,6 |
11,0 |
Cooling water flow rate |
m3/hod |
17,272 |
4,492 |
19,438 |
4,428 |
Draught behind boiler |
Pa |
151,0 |
25,0 |
150,0 |
25,0 |
Ambient temperature |
°C |
26,0 |
23,0 |
27,0 |
24,0 |
Relative air humidity |
% |
37,0 |
38,0 |
41,0 |
41,0 |
Barometric pressure |
kPa |
99,20 |
99,30 |
99,07 |
99,22 |
Oxygen O2 |
% |
7,59 |
10,37 |
7,17 |
11,20 |
Carbon dioxide CO2 |
% |
11,46 |
9,61 |
12,15 |
8,88 |
Carbon monoxide CO |
ppm |
82 |
133 |
101 |
173 |
Higher hydrocarbons OGC |
ppm |
6 |
5 |
3 |
6 |
Nitrogen dioxides Nox |
ppm |
74 |
61 |
93 |
56 |
Dust |
mg/m3 |
30 |
30 |
45 |
54 |
Carbon monoxide CO |
mg/m3 |
87 |
182 |
101 |
246 |
Higher hydrocarbons OGC |
mg/m3 |
3 |
3 |
2 |
4 |
Nitrogen dioxides Nox |
mg/m3 |
124 |
129 |
153 |
128 |
Dust |
mg/m3 |
24 |
32 |
25 |
48 |
Mass flow rate gases |
kg/sec |
0,236 |
0,064 |
0,224 |
0,070 |
Stoichiometric oxygen value |
m3/kg |
0,958 |
0,957 |
0,832 |
0,830 |
Stoichiometric air value |
m3/kg |
4,560 |
4,558 |
3,962 |
3,951 |
Stoichiometric volumeof dry combustion products |
m3/kg |
4,449 |
4,447 |
3,882 |
3,872 |
Stoichiometric air multiple |
|
1,56 |
1,99 |
1,51 |
2,19 |
Volume of dry combustion products, actual |
m3/kg |
7,388 |
8,843 |
6,191 |
8,481 |
Volume of H2O in the combustion air |
m3/kg |
0,087 |
0,098 |
0,089 |
0,174 |
Volume of H2O in the combustion produts |
m3/kg |
0,942 |
0,953 |
0,935 |
0,953 |
Maximum volume CO2 |
% |
19,01 |
19,01 |
19,40 |
19,40 |
Loss of sensible heat of combustion products (chimney) |
% |
4,7 |
3,3 |
4,7 |
3,3 |
Loss of gas underburning |
% |
0,0 |
0,1 |
0,0 |
0,1 |
Loss of mechanical underburning |
% |
0,0 |
0,1 |
0,3 |
0,6 |
Loss of heat transfer into the environment |
% |
0,6 |
1,4 |
0,5 |
1,2 |
Total loss |
% |
5,3 |
4,9 |
5,4 |
5,1 |
Efficiency – indirect method |
% |
94,7 |
95,1 |
94,6 |
95,0 |
Heat input |
kW |
363,0 |
85,2 |
371,4 |
89,0 |
Heat capacity |
kW |
345,8 |
81,4 |
354,5 |
85,2 |
Uncertainty of determining heat capacity |
% +/- |
14,5 |
3,4 |
14,9 |
3,6 |
Efficiency – direct method |
% |
95,3 |
95,5 |
95,4 |
95,7 |
Capacity / rated output |
% |
98,8 |
23,3 |
101,6 |
24,7 |
|