Abstract:An experimental study of the gas-solid flow dynamics in the high-flux CFB riser was accomplished by analysing the scaling regions from solid concentration signals collected from a 76 mm internal diameters and 10 m high riser of a circulating fluidized bed (CFB) system. The riser was operated at 4.0 to 10.0 m/s gas velocity and 50 to 550 kg/m 2 s solids flux. Spent fluid catalytic cracking (FCC) catalyst particles of 67 µm mean diameter and 1500 kg/m 3 density together with 70% to 80% humid air was used. Solid … Show more
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