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Dense-phase fluidized beds cyclones

Bed components in a dense-phase fluidized bed include the gas distributor, cyclone, dipleg, heat exchanger, expanded section, and baffles, as shown in Fig. 9.4. The basic function of each component in a fluidized bed is described in the following. [Pg.376]

A dense phase fluidized bed generally consist of a gas distributor, a cyclone, a dipleg, a heat exchanger, an expanded section, and baffles [44]. A schematic representation of a dense phase fluidized bed reactor is shown in Fig 10.3. [Pg.873]

As the gas velocity is increased beyond 17 a point is reached at which the particles are transported out of the bed altogether either in dense-phase or in dilute-phase pneumatic transport the velocity at which this occurs is called the transport velocity, C/tr- In order to maintain a constant inventory of particles in the bed at velocities in excess of 7tr it is necessary to recycle them via external cyclones and a standpipe, a geometry known as a circulating fluidized bed. A comprehensive review of the literature on circulating systems has been given by Grace et al. (1997), and the subject is also dealt with in Chapter 19 of this handbook. [Pg.151]

Fluidization occurs in stationary (segregation of bed and free board), turbulent (circulating fluid bed), and forced dense-phase (transport reactor) mode. All systems require hot gas cyclones either to recycle entrained particles back into the fluid bed or just to separate them from the product gas. [Pg.226]


See other pages where Dense-phase fluidized beds cyclones is mentioned: [Pg.436]    [Pg.874]    [Pg.1010]    [Pg.1011]    [Pg.1013]    [Pg.1014]    [Pg.247]    [Pg.573]    [Pg.975]    [Pg.900]    [Pg.42]    [Pg.160]    [Pg.874]    [Pg.209]    [Pg.174]    [Pg.2]    [Pg.596]    [Pg.264]   
See also in sourсe #XX -- [ Pg.376 ]




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