Mixing of nanoparticle agglomerates in fluidization using CFD-DEM at ABF and APF regimes

[Display omitted] •Solid mixing in nano-particle agglomerates fluidized bed was studied by CFD-DEM.•CUDA platform was used for solving solid-phase equations on GPU in parallel.•Void fraction and bed homogeneity were investigated for both APF and ABF regimes.•Axial and radial dispersion coefficients were studied for both APF and ABF regimes.•Lacey mixing index was studied for both APF and ABF regimes. Mixing of nanoparticle agglomerates in a fluidized bed was investigated by CFD-DEM. A parallel program was used that simultaneously uses the computational resources of GPU and CPU on a single computer. The bed expansion obtained from simulation was compared with experimental and good agreement was observed. Bed expansion in agglomerate particulate fluidization (APF) was 2 to 5 times the initial bed height and final bed expansion in agglomerate bubbling fluidization (ABF) was 1 to 2 times the initial bed height by changing the gas velocity from 2 to 4 and 4 to 8cm/s for APF and ABF regimes respectively. Gas volume fraction distribution was investigated for both APF and ABF regimes, which showed a more uniform distribution in APF. Increasing the gas velocity led to a more homogenous in the APF bed but it did not change the homogeneity of the ABF bed. Besides, the axial and radial dispersion coefficients in ABF were greater than those in APF. Axial dispersion coefficient varied from 2×10−6 to 4×10−5m2/s. Lacey mixing index was investigated in both APF and ABF regimes and it showed that the quality of mixing in ABF was better than APF.