Etude d'un procédé de gazéification de biomasse en ambiance ...

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ANNEXES ________________________________________________________________________________________________________________ favorise la formation de CO et H2 ainsi que le vaporéformage du CH4 et la destruction des goudrons. Figure XVI-5 : Schéma d’un gazéifieur à flux entraîné : Shell (ADEME, 2004). XVI - 7 - Récapitulatif des études et des réalisations Technologies de gazéification Lits fixes à contre-courant Lits fixes à co- courant Lits fluidisés bouillonnants Les études (Ballerini et Alazard- Toux, 2006) Wellman, Volund, Bioneer DTU, TKE, Biomass Engineering, Fluidyne, DeLacotte EPI, Carbona, ASCAB Lits circulants FICFB, Lurgi, Foster Weeler Les réalisations (ADEME, 2004) Sasol (Afrique du Sud), DCG (Etats- Unis), Shanxi (Chine) Nippon Steel (Japon), Xylowatt (Belgique) HTW (Winkler) (Japon, Allemagne), Biosyn, Carbona (Finlande, USA) Lurgi CFB (Allemagne, Australie, Hollande), Foster Wheeler (Finlande, Suède, Portugal), TPS Termiska (Suède, Italie, Royaume-Uni, Brésil) 269
ANNEXES ________________________________________________________________________________________________________________ Lits circulants à doubles corps Réacteur à flux entraînés Ferco Battelle Texaco, Choren, Future Energy, Lurgi MPG, Shell Shell, Noell (Hollande, Angleterre), Lurgi MPG Tableau XVI-1 : Récapitulatif des sociétés ayant étudié et réalisé des réacteurs de gazéification. XVII - ANNEXE « COMPOSITION DES VERRES FNOC 57 ET FN1C 101 » XVII - 1 - Caractéristiques du verre FNOC 57 XVII - 2 - Caractéristiques du verre FNIC 101 270
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Résumé __________________________
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Table des matières _______________
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Glossaire _________________________
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Introduction ______________________
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I -Le contexte énergétique et env
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II -Etat de l’art des procédés
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III -Matériels et méthodes ______
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IV -Les résultats expérimentaux _
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V -Modélisation des transitoires t
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VI -Etude technico-économique d’
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VII -Conclusion générale et persp
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VII - Conclusion générale et pers
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VIII -Bibliographie _______________
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