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Catalytic ozone decomposition reaction was used to study the performance of a 76mm i.d. and 10.2m high gas–solid circulating fluidized bed (CFB) riser reactor. Optical fiber probes and an ultraviolet (UV) ozone analyzer were used to obtain comprehensive information about local solid holdup and ozone concentration profiles at different axial and radial positions. The operating conditions were at superficial...
Rotational asymmetric distribution of reactant (ozone) concentration and its evolution along with the gas-solid reactive flow were studied in a 76mm i.d., 10.2 m high circulating fluidized bed (CFB) riser reactor. The superficial gas velocity ranged from 3 to 5 m/s and the solids circulation rates were 50 and 100kg/(m 2 s). Experimental results show that the asymmetry of reactant distribution...
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