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

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Bibliographic revision<br />

scrubbing and product gas compression would have an analogous efficiency as<br />

low as 80-85%, <strong>de</strong>pending on capacity and <strong>de</strong>sign.<br />

Atmospheric gasifiers have the following significant features:<br />

- For gas turbine applications the product gas is required to be sufficiently clean<br />

for compression before the turbine. Suggested specifications are given <strong>la</strong>ter.<br />

For engine applications the gas quality requirements are less onerous and<br />

pressure is not required.<br />

- Atmospheric systems have a potentially much lower capital cost at smaller<br />

capacities of below 30 MW e as discussed above.<br />

Gas compositions and heating values are not significantly different for either system<br />

(Bridgwater, 1995).<br />

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

2.3.4 Influence of the oxidizer<br />

It is well-known that the heating value and the H 2 content of syngas are higher when<br />

gasification is ma<strong>de</strong> with steam than it is ma<strong>de</strong> with air (Javier et al., 1999).<br />

Table 2.7 shows experimental results of wood gasification using different types of<br />

oxidizers.<br />

Table 2.7 - Influence of the oxidizer in the final composition of syngas.<br />

Oxidizing agent<br />

Composition (% vol, dry base) HHV<br />

H (MJ/m 3 2 CO CO 2 CH 4 N 2<br />

)<br />

Reference<br />

Air (downdraft) 17 21 13 1 48 5.7 (Bridgwater, 1995)<br />

Air (updraft) 11 24 9 3 53 5.5 (Bridgwater, 1995)<br />

O 2 (downdraft) 32 48 15 2 3 10.4 (Bridgwater, 1995)<br />

Air (BFB) 9 14 20 7 50 5.4 (Bridgwater, 1995)<br />

Air (CFB) 14.1 18.7 14.7 3.5 47.7 n.d. (Mehrling et al. , 1989)<br />

Air (BFB) 9.5 18 13.5 4.5 45 n.d. (Narvaez, 1996)<br />

Steam (CFB) 34.2 27.2 22.7 11.1 4.8 n.d. ( Fercher et. al., 1998)<br />

Steam (BFB) 52 23 18 7 n.d. n.d. (Herguido et. al., 1992)<br />

It is verified that the use of steam or O 2 as oxidizer agent increases remarkably the<br />

production of H 2 and CO reflecting a significant increase of the syngas heat value. In<br />

the case of the fluidized bed reactors, an increase of the methane yields is also verified<br />

using steam as oxidizer.<br />

38

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