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Etude de la combustion de gaz de synthèse issus d'un processus de ...

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Chapter 2<br />

Table 2.8 shows a comparison performed by Javier et al. (1999) based on results from<br />

Herguido et al. (1992), Javier et al. (1997) and Narváez et al. (1996) in or<strong>de</strong>r to<br />

<strong>de</strong>termine the effect of gasifying agent on other results like tar content in the produced<br />

gas. Three basic ratios were used for comparison of results using different gasifying<br />

agents in a bubbling fluidized bed gasifier running with small chips of pine:<br />

- Equivalence ratio (φ) for air;<br />

- Gasifying ratio (GR) [(H 2 O+O 2 )/Biomass (kg/h)/(kg dry-ash free/h)], for steam-<br />

O 2 mixtures;<br />

- Steam to biomass ratio (SB) [H 2 O/Biomass (kg/h)/(kg dry-ash free/h).<br />

Table 2.8 – Effect of gasifying agent on syngas composition<br />

Parameter Air (φ=0.3) Steam/O 2 GR = 0.9 Steam SB=0.90<br />

tel-00623090, version 1 - 13 Sep 2011<br />

H 2 (vol.% dry basis) 8-10 25-30 53-54<br />

CO (vol.% dry basis) 16-18 43-47 21-22<br />

LHV (MJ/m 3 , dry basis) 4.5-6.5 12.5-13.0 12.7-13.3<br />

Ygas (m 3 , dry basis/kg daf) 1.7-2.0 1.0-1.1 1.3-1.4<br />

Y tar (g/kg daf) 6-30 8-40 70<br />

Tar (g/m 3 ) 2-20 4-30 30-80<br />

Gasification with air produces a higher syngas yield. Tar yields are quite different<br />

between the gasifying agents being the lowest values obtained with air.<br />

2.4. Concluding remarks about biomass gasification<br />

Gasification is a versatile thermochemical conversion process which produces a gas<br />

mixture of H 2 , CO and CH 4 the proportions being <strong>de</strong>termined by the use of air, oxygen<br />

or steam as the gasification medium, with a concomitant range of heat values, low (4–6<br />

MJ/Nm 3 ), medium (12–18 MJ/Nm 3 ) and high (40 MJ/Nm 3 ). Key parameters for<br />

successful gasification are the feedstock properties (moisture, ash, alkalis and<br />

vo<strong>la</strong>tiles) and feedstock pre-treatment (drying, particle size, fractionation and leaching).<br />

Gasifiers are of two main types, fixed bed and fluidized bed, with variations within each<br />

type and specific characteristics which <strong>de</strong>termine the need for and extent of feedstock<br />

preparation/pre-treatment.<br />

For use in gas engines gas produced from a fixed bed, downdraft gasifier provi<strong>de</strong>s a<br />

low tar gas, with a high particu<strong>la</strong>tes loading: as tar is a major contaminant for engine<br />

operation and particu<strong>la</strong>tes can be re<strong>la</strong>tively easily removed, this system is consi<strong>de</strong>red<br />

best for fuelling gas engines. Extensive <strong>de</strong>velopment of wood gas-fuelled IC engines,<br />

39

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