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- W2014271921 abstract "Experimental gas hold-up data in a two-dimensional spouted bed, 22 mm × 220 mm × 1250 mm, at superficial gas velocities between 0.34 and 3.43 m s−1, operating continuously with respect to the gas flow and batchwise with respect to the liquid and using a single-nozzle gas sparger are presented. The effect of the static liquid height, nozzle diameter and superficial gas velocities on gas hold-up were studied. The gas hold-up was measured directly by using the bed expansion technique. The effect of nozzle diameter on the gas hold-up was found to be insignificant. Results were well correlated by the following equation eg = 0. 182 Ug0.584 H−0.288 with an average deviation of less than 1%. The correlation is compared with others available in the literature." @default.
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- W2014271921 date "1991-12-01" @default.
- W2014271921 modified "2023-09-26" @default.
- W2014271921 title "Gas hold-up in a bidimensional two-phase spouted bed" @default.
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- W2014271921 doi "https://doi.org/10.1016/0300-9467(91)85018-q" @default.
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