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What information does basic fuel characterisation provide?
Date posted:
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Post Author
espadmin
1. Background
The
concepts of fuel characterisation are outlined in Combustion File 48 “What is pulverised fuel characterisation?”.
Two levels of pulverisation fuel characterisation are identified:
- Basic pulverised fuel characterisation
- Advanced pulverised fuel characterisation
This combustion file develops information on the former and commences to provide examples for a range of solid fuels for pulverised fuel firing.
2. Basic Fuels Characterisation
The basic fuel characterisation techniques, described in details in Combustion File 24 How do I make a basic combustion characterisation of a Biofuel?, focuses on the following main physical-chemical and combustion characteristics:
- [GLOSS]proximate analysis[/GLOSS]: moisture, volatile matter, fixed carbon and ash content
- [GLOSS]ultimate analysis[/GLOSS]: carbon, hydrogen, nitrogen, sulphur and oxygen
- chlorine content: important where plastic wastes and some biomass, such as straw, are included
- [GLOSS]higher calorific value[/GLOSS]
- bulk density
- particle size distribution
- ash composition
- [GLOSS]ash fusibility[/GLOSS] defined by ash fusion temperatures: [GLOSS]initial deformation temperature[/GLOSS], [GLOSS]hemisphere temperature[/GLOSS] and [GLOSS]flow temperature[/GLOSS],
- [GLOSS]heavy metals analyses[/GLOSS].
3. Basic fuel characterisation example
An example of the basic fuel characterisation can be seen on Table 1, from [1].
Table 1a. Proximate analysis.
%wt as received |
Bituminous |
Pine |
Dry |
RDF-Refuse |
Moisture |
1.7 |
7.3 |
4.0 |
4.66 |
Volatile matter |
34.0 |
76.2 |
52.0 |
72.78 |
Fixed carbon |
59.3 |
13.9 |
13.0 |
13.66 |
Ash |
5.0 |
2.6 |
31.0 |
8.9 |
Table 1b. Ultimate analysis.
%wt dry basis (incl.ash) |
Bituminous |
Pine |
Dry |
RDF-Refuse |
Carbon |
79.2 |
50.6 |
30.9 |
43.19 |
Hydrogen |
4.7 |
5.6 |
4.6 |
6.75 |
Nitrogen |
1.8 |
0.1 |
4.5 |
0.63 |
Sulphur |
0.9 |
0.04 |
1.1 |
trace |
Oxygen |
7.6 |
40.84 |
26.5 |
38.79 |
Chlorine |
0.7 |
0.02 |
0.1 |
1.3 |
Table 1c. Calorific value.
Bituminous |
Pine |
Dry |
RDF-Refuse |
|
MJ/kg |
79.2 |
50.6 |
30.9 |
43.19 |
Higher
calorific value:
- British Standard Methods (BS:1016:part 5: 1977) using bomb calorimeter
- Calculated based on the ultimate analysis as an example [MJ/kg] = 109.6*(C/3+H+S/8-O/8)-0.8817
Table 1d. Bulk density.
Bituminous |
Pine |
Dry |
RDF-Refuse |
|
Kg/m3 |
603.3 |
182 |
610 |
64.1 |
Table 1d. Particle size distribution.
Particle |
Percentage |
|
Bituminous
|
<188 mm |
100 |
Pine sawdust |
<1.78 mm |
100 |
Dry sewage sludge |
<300 mm |
100 |
RDF-Refuse derived fuel |
<564 mm |
100 |
Table 1e. Ash composition.
%wt as oxide |
Bituminous |
Pine |
Dry |
Refuse |
SiO2 |
34.1 |
18.1 |
33.6 |
39.8 |
Al2O3 |
24.9 |
2.5 |
15.6 |
23.7 |
CaO |
8.1 |
55.7 |
22.2 |
22.9 |
P2O5 |
1.2 |
2.1 |
16.7 |
1.0 |
Fe2O3 |
21.1 |
2.4 |
3.6 |
2.3 |
TiO2 |
0.7 |
0.3 |
1.3 |
2.1 |
MgO |
1.9 |
6.3 |
2.3 |
2.7 |
Na2O |
2.1 |
1.9 |
0.5 |
2.0 |
K2O |
1.0 |
8.3 |
1.1 |
1.9 |
SO3 |
4.9 |
2.4 |
3.1 |
1.6 |
Table 1f. Ash fusion temperature.
oC |
Bituminous |
Pine |
Dry |
Refuse |
IDT |
1080 |
1060 |
1110 |
1150 |
HDT |
1170 |
1150 |
1220 |
1170 |
FT |
1300 |
1230 |
1270 |
1220 |
IDT
– Initial Deformation Temperature, HDT – Hemisphere Temperature, FT – Flow Temperature
Table 1g. Heavy metals – trace element concentration.
ppm by weight |
Bituminous |
Pine |
Dry |
Refuse |
Pb |
20 |
<3 |
211 |
50 |
Cd |
<1 |
<1 |
2 |
<1 |
Hg |
<2 |
<2 |
<2 |
<2 |
V |
7 |
<1 |
12 |
4 |
Zn |
15 |
9 |
567 |
85 |
Ni |
3 |
<2 |
32 |
2 |
Mn |
53 |
93 |
209 |
57 |
Fe |
2940 |
<6 |
5400 |
768 |
As |
5 |
14 |
10 |
5 |
Mo |
<2 |
<2 |
5 |
<2 |
Al |
146 |
15 |
11700 |
1600 |
Cu |
23 |
3 |
829 |
35 |
Co |
<2 |
<2 |
3 |
<2 |
Cr |
<2 |
3 |
62 |
8 |
SO-24 |
10300 |
209 |
28800 |
3450 |
Sources
[1] Abbas, T., Costen, P. Glaser, K., Hassan S. Lockwood, F. Ou, J.-J. Combined
Combustion of Biomass, Municipal Sewage Sludge and Coal in a Pulverised Fuel
Plant. In Hein, K.R.G. (ed.), Clean Coal Technology Programme 1992-1994 Vol. II,
Combined Combustion of Biomass/Sewage Sludge and Coals: Final Reports,
EC-Research Project: APAS-Contract COAL-CT92-0002, Institute for Process
Engineering and Power Plant. (1994).