Gas/solids flow patterns in a 30.5-cm-diameter circulating fluidized bed

ABSTRACT Tests were conducted in a 30.5-cm-diameter riser with 76 μm FCC catalyst to determine the degree of gas/solid contacting in the “fast-fluid bed” regime. Data were obtained at superficial gas velocities of 3.7 to 6.1 m/s and solid fluxes of 98 to 195 kg/s-m 2 . The conveying gas was air at ambient temperature and 103 kPa. Data were obtained on axial pressure profiles, particle velocity and mass flux as a function of radial and axial position, radial and axial gas dispersion, and solids residence time distributions. Density and voidage profiles were calculated from these data. Radial and axial gas dispersion coefficients were determined from steady-state helium tracer tests. The radial gas dispersion coefficient was found to be in the range of 25.8 to 64.5 cm 2 /s with an average value of 38.7 cm 2 /s. The axial gas dispersion was so small, 2 /s as to be negligible compared to convective gas flow. Solids residence time distributions obtained from pulse injections of NaCl tracer showed considerable backmixing of solids.