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Generalized fluidization diagram

The load characteristic of circulating fluidized bed boilers is closely related to the gas-solid flux through the combustor. Thus, choice of coal size and the proper gas-solid separator deserves attention. Generally, the fraction of particles below 0.1 mm is smaller than 10%, which could be removed only by a cyclone separator, while the major fraction of coarser particles could be easily separated by inertia or gravity (Li and Kwauk, 1981). The diagram of ash balance for a circulating fluidized bed boiler, shown in Fig. 22, can... [Pg.356]

Figure 24 Generalized fluidization diagram with homogeneous drag (air-FCC... Figure 24 Generalized fluidization diagram with homogeneous drag (air-FCC...
Figure 25 Generalized fluidization diagram with EMMS drag coefficient (air-FCC particle system, dp = 75(im, />p=1500 kg/m />g=1.3kg/m //g=1.8x 10 Pa s, Ut=0.2184 m/s) (Ullah et al, 2013b). Figure 25 Generalized fluidization diagram with EMMS drag coefficient (air-FCC particle system, dp = 75(im, />p=1500 kg/m />g=1.3kg/m //g=1.8x 10 Pa s, Ut=0.2184 m/s) (Ullah et al, 2013b).

See other pages where Generalized fluidization diagram is mentioned: [Pg.722]    [Pg.604]    [Pg.75]    [Pg.482]    [Pg.484]    [Pg.257]    [Pg.69]    [Pg.465]    [Pg.482]    [Pg.484]    [Pg.180]    [Pg.1397]    [Pg.146]    [Pg.1405]    [Pg.1405]    [Pg.84]    [Pg.84]    [Pg.2462]    [Pg.1404]    [Pg.1404]    [Pg.84]    [Pg.84]    [Pg.132]    [Pg.230]    [Pg.261]    [Pg.262]    [Pg.319]    [Pg.1009]   
See also in sourсe #XX -- [ Pg.261 , Pg.263 , Pg.265 , Pg.265 ]




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