Gas–solid fluidization has a wide range of industrial applications like catalytic reactions, combustion, gasification, etc. In a number of these applications, there is particle size reduction during the operation leading to severe entrainment and limitation of operating velocity. The various problems associated with particles of different sizes or changing particles sizes could be overcome by adopting tapered beds in fluidization operation. In the present investigation, the fluidization phenomenon in tapered beds has been critically assessed through experimental investigations using particles of different sizes and materials and wide range of apex angles of the vessels. The effect of particle size and apex angle on the fluidization behaviour is clearly brought out which has not been reported so far in literature. The importance of compressive force existing in tapered beds is highlighted. In addition, correlations for all hydrodynamic characteristics, viz. critical fluidization velocity, minimum velocity for full fluidization, maximum velocity for defluidization, peak pressure drop, fluctuation ratio, compressive force, and hysteresis have been developed some of which are proposed for the first time. La fluidisation gaz-solide revet un vaste eventail d'applications industrielles comme les reactions catalytiques, la combustion, la gazeification, etc. Pour un certain nombre deces applications, il y a une reduction granulometrique durant l'activite menant a un entrainement eta une limitation intenses de la vitesse de fonctionnement. Les divers problemes lies aux particules de dimensions differentes ou aux dimensions de particules changeantes pourraient etre surmontesen adoptant les lits coniques dans les activites de fluidisation. Dans le cadre de la presente etude, lephenomene de fluidisation dans les lits coniques a ete evalue de facon critique au moyen deverifications experimentales employant des particules de dimensions et de matieres differentes et d'un vaste eventail d'angles de sommet de fluidiseurs. L'effet de la dimension des particules et del'angle des sommets sur le comportement de la fluidisation est nettement mis en evidence, ce quin'a pas ete souleve a venir jusqu'ici dans la documentation. L'importance de la force decompression qui existe dans les lits coniques est mise en evidence. De plus, les correlations relativement a l'ensemble des caracteristiques hydrodynamiques, c.-a-d. la vitesse de fluidisation critique, la vitesse minimale de fluidisation complete, la vitesse maximale de defluidisation, la chute des pics de pression, le taux de fluctuation, la force de compression et l'hysteresis, ont ete elaborees, certaines d'entre elles etant avancees pour la premiere fois.