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

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Bibliographic revision<br />

Circu<strong>la</strong>ting Fluidized bed (CFB)<br />

Circu<strong>la</strong>ting FB gasifiers are able to cope with high capacity throughputs and are used in<br />

the paper industry for the gasification of bark and other forestry residues.<br />

The bed material is circu<strong>la</strong>ted between the reaction vessel and a cyclone separator,<br />

where the ash is removed and the bed material and char returned to the reaction<br />

vessel. Gasifiers can be operated at elevated pressures, the advantage being for those<br />

end-use applications where the gas is required to be compressed afterwards, as in a<br />

gas turbine.<br />

Gas + contaminants<br />

Gas<br />

Cyclone<br />

Fluidized bed<br />

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

Biomass<br />

Grate<br />

Ashes<br />

Oxidant<br />

speed 5-10 m.s -1<br />

Tar + inert<br />

Figure 2.6 - Circu<strong>la</strong>ting fluidized bed gasifier<br />

The advantages of such gasifier are (Bridgwater and Evans, 1993):<br />

- Suitable for rapid reactions;<br />

- High heat transport rates possible due to high heat capacity of bed<br />

material;<br />

- High conversion rates possible with low tar and unconverted carbon.<br />

. The disadvantages are (Bridgwater and Evans, 1993):<br />

- Temperature gradients occur in direction of the solid flow;<br />

- Size of fuel particles <strong>de</strong>termine minimum transport velocity; high velocities<br />

may result in equipment erosion;<br />

- Heat transfer less efficient than bubbling fluidized bed.<br />

28

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