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- W2068591924 abstract "A mathematical model has been developed to describe the solids transport in a gas lift system, with a fluidized bed as mixing zone. Its validity was checked in gas lifts with different transport heights, using alumina and uranium dioxide spheres as solids. The two solid phase parameters used in the model are the slip velocity Δμ between gas and solids and an empirical coefficient α, which accounts for hindered settling of the particles in the transport tube. These parameters are determined by the experimental procedure. From the results obtained in the proposed system, it could be deduced that the particles are transported in “clusters” due to the attractive forces between them and also due to the fact that “dune” transport cannot be avoided in this low energy system. Compared to classical transport devices, high transport efficiencies are thus obtained. Finally, an interesting application of the gas lift system as an internal mixing device of dissimilar solids with high demixing tendencies in a fluidized bed system is proposed." @default.
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- W2068591924 date "1972-04-01" @default.
- W2068591924 modified "2023-09-26" @default.
- W2068591924 title "Vertical pneumatic conveyer with a fluidized bed as mixing zone" @default.
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- W2068591924 doi "https://doi.org/10.1016/0032-5910(72)80034-2" @default.
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