EasyManua.ls Logo

Seitron CHEMIST 600 - ANNEX C - Coefficients of the Fuels and Formulas

Seitron CHEMIST 600
200 pages
Print Icon
To Next Page IconTo Next Page
To Next Page IconTo Next Page
To Previous Page IconTo Previous Page
To Previous Page IconTo Previous Page
Loading...
187
K600000000SE 030804 011018
ANNEX C
Coefficients of the fuels and Formulas
The following chart, derived from standard UNI 10389-1, lists the coefficients of the memorised fuels, used for
calculating losses and efficiencies.
Details of the coefficients of the fuels:
CO2 t: The value of CO
2
generated by combustion in stoichiometric condition, i.e. without excess Oxygen
and therefore maximum.
A1, A2, B: Also please have a look at the Siegert formulas from the European standard EN50379-1 (in the
following).
A1 is the parameter in the Siegert Formula when the O
2
measurement is available.
A2 is used when the CO
2
measurement is available.
Note: - Please also consider that in the U.S. usually the A1 parameter is the same as the
'European' A1 BUT divided by 2.
- For Germany coefficients A1 and A2 are swapped.
Flue gas heat losses are calculated from measured oxygen content according to the relationship:
Coefficients for calculating combustion efficiency
Fuel A1 A2 B CO2t
(%)
PCI
(KJ/Kg)
PCS
(KJ/Kg)
M air
(Kg/Kg)
M H
2
O
(Kg/Kg)
V dry gas
(m
3
/Kg)
Natural gas 0,660 0,380 0,0100 11,70 50050 55550 17,17 2,250 11,94
Propane 0,630 0,420 0,0080 13,90 45950 49950 15,61 1,638 11,11
L.P.G. 0,630 0,420 0,0080 13,90 45730 49650 15,52 1,602 11,03
Butane 0,630 0,420 0,0080 13,90 45360 49150 15,38 1,548 10,99
Diesel oil 0,680 0,500 0,0070 15,10 42700 45500 14,22 1,143 10,34
Fuel oil 0,680 0,520 0,0070 15,70 41300 43720 13,73 0,990 10,06
Propane air 0,682 0,447 0,0069 13,76 28250 30700 9,13 0,999 6,77
Biogas 0,719 0,576 0,0086 16,81 19200 21250 6,38 0,840 5,82
Pellets (8% RH) 0,740 0,670 0,0071 19,01 18150 19750 6,02 0,660 4,58
Wood (20% RH) 0,761 0,686 0,0089 18,93 15450 17170 5,27 0,700 4,01
Chipped wood 0,8020 0,785 0,0108 20,56 11950 13565 4,20 0,660 3,25
Coal 0,7620 0,691 0,0023 19,06 31400 32300 10,70 0,370 8,14
CO Off gas 0,775 1,164 0,0012 31,55 8610 8735 2,21 0,051 2,14
Olive pits 0,749 0,689 0,0065 19,33 18780 20309 6,290 0,626 4,79
Rice husk 0,777 0,768 0,007 20,738 12558 13633 4,065 0,440 3,152
Flue gas heat losses are calculated from measured carbon dioxide content according to the relationship:
CO conv: Conversion coefficient from ppm to mg/KWh. It can be expressed as a function of the gas density
(CO in this case) and the volume of the dry smoke.
NO conv: Same as CO conv, but for NO.
NOx conv: Same as CO conv, but for NOx.
SO2 conv: Same as CO conv, but for SO2.
PCI: Potere Calorifico Inferiore. Italian for LHV (Lower Heating Value).
PCS: Potere Calorifico Superiore. Italian for HHV (Higher Heating Value).
m H2O: Mass of the air produced (per each Kg of fuel) in the combustion in stoichiometric condition.
m Air: Mass of the air needed for combustion in stoichiometric condition.
V g.d.: Volume of dry smokes produced in the combustion.
q
A
= (t
A
- t
L
) x
A1
21 - O
2
+ B
q
A
= (t
A
- t
L
) x
A2
CO
2
+ B
Air index is calculated with the formula:
λ=21/(21-O
2
), where O
2
is the oxygen residual concentration in the combustion smokes.
Air excess is calculated with the formula:
e=(λ-1)*100

Table of Contents

Related product manuals