|
Class
|
|
D
|
E
|
F
|
0
|
|
Grade
|
|
Gas
Oil
|
Light
|
Medium
|
Heavy
|
|
|
|
|
Fuel
Oil
|
Fuel
Oil
|
Fuel
Oil
|
|
Gross
calorific value
|
- MJ/kg
|
46.60
|
43.02
|
42.46
|
41.83
|
|
|
- MJ/l
|
38.30
|
41.08
|
41.44
|
41.83
|
|
Nett
calorific value
|
- Md/kg
|
42.80
|
40.60
|
40.13
|
39.57
|
|
|
- MJ/l
|
35.95
|
38.77
|
39.17
|
39.37
|
|
Ultimate Analysis (dry basis):
|
|
Carbon
|
%
mass
|
86.1
|
85.6
|
85.6
|
85.4
|
|
Hydrogen
|
%mass
|
13.6
|
12.0
|
11.6
|
11.2
|
|
Sulphur
|
%
mass
|
0.3 |
2.2 |
2.6 |
3.0 |
|
Oxygen,
Nitrogen,
|
|
|
|
|
|
|
Ash
|
%
mass
|
- |
0.2 |
0.3 |
0.4 |
|
Stoichiometric
air requirements:
|
|
-
mass/mass fuel
|
|
14.595
|
14.064
|
13.908
|
13.797
|
|
-vol/massfuel
|
m3/kg
|
11.94
|
11.51
|
11.38
|
11.29
|
|
Sloichiometric
combustion products:
|
|
- CO2 |
%
vol
|
13.29
|
13.79
|
13.96
|
14.08
|
|
- H2O |
%vol
|
12.59
|
11.59
|
11.28
|
11.10
|
|
- N2 |
%
vol
|
74.10
|
74.49
|
74.60
|
74.64
|
|
- SO2
|
%vol
|
0.02
|
0.13
|
0.16
|
0.18
|
|
-
Water dewpoint 0C
|
50 |
50
|
50
|
50
|
|
-Acid
dewpoint 0C
|
127
|
143
|
154
|
160
|
|
-
C02 in dry products % vol
|
15.21
|
15.60
|
15.74
|
15.84
|
|
-
502 in dry products % vol
|
0.02
|
0.15
|
0.18
|
0.20
|
|
Theoretical flame temp. 0C
|
2022
|
2028
|
2028
|
2028
|
|
For more
information contact Mearsecroft
Created and updated by Spiders
Webs |