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

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Chapter 2<br />

o Oxygen;<br />

o Steam;<br />

o Other gases containing oxygen, such as CO 2 (Gañan et al., 2005).<br />

Gasifier heating:<br />

o Direct ;<br />

o Indirect.<br />

Heating value (McKendry, 2002b):<br />

o<br />

o<br />

o<br />

Low: 4 -6 MJ/Nm 3 (using air or air / steam);<br />

Medium: 12 -18 MJ/Nm 3 (using oxygen and steam);<br />

High: 40 MJ/Nm 3 , using hydrogen and hydrogenation.<br />

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

2.1.3 Gasification p<strong>la</strong>nt<br />

A gasification p<strong>la</strong>nt consists into three main units (McKendry, 2002a):<br />

o Gasification unit – the reactor,<br />

o Cleaning unit - filtration and cooling, and<br />

o Energy conversion unit.<br />

These are briefly <strong>de</strong>scribed in the following sections.<br />

2.1.3.1 Gasifier types<br />

A variety of biomass gasifier types have been <strong>de</strong>veloped. They can be grouped into<br />

four major c<strong>la</strong>ssifications: fixed-bed updraft, fixed-bed downdraft, bubbling fluidized-bed<br />

and circu<strong>la</strong>ting fluidized bed. Differentiation is based on the means of supporting the<br />

biomass in the reactor vessel, the direction of flow of both the biomass and oxidant,<br />

and the way heat is supplied to the reactor (Rampling and Gill, 1993). Table 2.1 lists<br />

the most commonly used configurations.<br />

23

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