Gas-solid fluidized bed separation expands the choices of highly efficient dry coal beneficiation methods The hydrodynamics of 0 3-0 15 mm large Geldart B magnetite powder were studied using a combination of experimental and numerical methods to optimize the design of the solid medium used in the fluidized bed The results show that the Syamlal-O Brien drag model is suitable for simulating the bed and it is verified that simulated and experimental results are consistent with each other If the static bed height is no more than 300 mm then the bed height has minimal effect on the fluidization characteristics As the superficial gas velocity increases the bed activity is improved However at the same time the uniformity and stability of the bed drop Therefore the gas velocity should be adjusted to no more than 2 OUmf The density of the Geldart B bed is uniform and stable which indicates a relatively high fluidization quality Furthermore compounded medium solids consisting of <0 3 mm magnetite powder with a 03-0 15 mm particle content of 65 25% and <1 mm fine coal were used in a pilot gas-solid fluidized bed of 5-10 ton/h capacity The pilot bed was used to separate 50-6 mm coal This test resulted in the coal ash content being reduced from 23 74% to 11 79% with a probable error E of 007 g/cm(3) and a recovery efficiency of 98 26% This indicates that the bed has good separating performance Nevertheless to increase the applicability of the separating bed a further study emphasizing a decrease in the lower size limit of the magnetite powder should be performed (C) 2010 Elsevier B V All rights reserved