22
www.ecoflam-burners.com
EN
420010463703
EXHAUST GAS TEST
Q
F
=
Q
N
=
1000
= 1136 kW
Volumetric gas flow rate at STP:
v
Bn
=
Q
N
=
1000
= 125 m
3
/h
Volumetric gas flow rate in operating
condition:
v
BB
= v
Bn
T
=
p
n
=
= 125
273+15 1013,25
= 123,9 m
3
/h
To ensure an economically efficient and
trouble-free operation of the system it will
be necessary to adjust the burner
specifically in accordance with the furnace
system. This is achieved by means of a
fuel-combustion air compound control unit
which adjusts the burner to ensure a
proper combustion. Exhaust gas tests are
required for this purpose.
The percentage CO2 and O2 and the
exhaust gas temperature will have to be
measured to determine the efficiency and
combustion quality.
Prior to any measurement make sure to
check the boiler and exhaust gas system
for absence of leaks.
Secondary air will falsify the measured
results
Check that the exhaust gases have a
residual oxygen (O2) content as low as
possible and a carbon dioxide (CO2)
content as high as possible.
The carbon monoxide content of the
exhaust gases must be below the currently
applicable specifications in all load stages.
In the fuel oil combustion mode the
permissible soot number in the exhaust
gas is not allowed to be exceeded
DETERMINING THE VOLUMETRIC GAS
FLOW RATE
The thermal furnace output of a boiler (QF)
is the amount of heat supplied with the gas
in a unit of time.
When taking the burner into operation the
volumetric fuel flow rate should be
selected according to the nominal thermal
capacity of the boiler.
Example:
Nom. thermal output
Q
N
1000 kW
Boiler efficiency
n
K
0,88
Calorific value of gas Hu
9,1 kWh/m
3
Gas pressure
p
U
100 mbar
Barometer reading
p
amb
980 mbar
Gas temperature
relative
t
gas
15°C
Gas temperature
absolute
T
(t
gas+
273)
Standard atmosferic
pressure
p
n
1013 mbar
0,88
n
K
H
u
*n
K
9,1*0,88
273
p
amb
+ p
u
273
980+100
Recommended combustion parameters
Ratio between O
2
- and CO
2
-
for natural gas H (CO
2
max = 11,7%)
Ratio between O
2
- and CO
2
-
for light oil EL (CO
2
max = 15,40%)
Ratio between O
2
- and CO
2
-
for heavy oil S (CO
2
max = 15,60%)
O
2
= 21 CO
2
max - CO
2
gem = %
CO
2
max
WARNING:
if the installation is above sea level the output of the burner
vary base on the diagram.
The regulation of the burner in this case shall take into account the
reduced power of the burner due to the missing air.
Fuel
Recommended
(%) CO2
Recommended
(%) O2
Natural gas
10 ÷ 9
3,1 ÷ 4,8
Light oil
13 ÷ 11,5
3,3 ÷ 5,3
Heavy oil
12,5 ÷ 11
4,2 ÷ 6,2
0
0
500
1000
1500
2000
2500
3000
3500
4000
4500
5000
5
10
15
20
25
30
35
40
45
50
Mean
air
pressure
vs
.
a
l
titude
above
sea
-l
eve
l
F
an
capacit
y
reduced
b
y [%]
A
l
titude
o
f
insta
ll
ation
site
[
m
]
CO
2
gem = % CO
2
measured on dry flue gases
Summary of Contents for 3142132
Page 3: ...3 www ecoflam burners com EN 420010463703 CONFORMITY DECLARATION ...
Page 34: ...34 www ecoflam burners com EN 420010463703 APPENDIX Fluidics nozzle chart ...
Page 35: ...35 www ecoflam burners com EN 420010463703 APPENDIX Fluidics nozzle chart ...
Page 36: ...36 www ecoflam burners com EN 420010463703 APPENDIX Fluidics nozzle chart ...
