1984
DOI: 10.1007/bf00261327
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A new method to measure particle turbulent dispersion using laser doppler anemometer

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Cited by 8 publications
(7 citation statements)
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“…An extensive review is not possible here, but it must be emphasized at the outset that almost all this work is confined to particle concentrations far below the range of interest from the point of view of particle transport systems. Many experiments have been described on vertical pipe flows with suspended spherical particles at mass loadings ranging up to about 6 (see, for example, So0 et al, 1960; Lee and Durst, 1982;Arnason and Stock, 1984;Tsuji et al, 1984). Mass loading is defined as the mass ratio of solids to gas, and values of 50 or higher are typically encountered in applications such as FCC risers.…”
Section: Dusty Gas Limitmentioning
confidence: 99%
“…An extensive review is not possible here, but it must be emphasized at the outset that almost all this work is confined to particle concentrations far below the range of interest from the point of view of particle transport systems. Many experiments have been described on vertical pipe flows with suspended spherical particles at mass loadings ranging up to about 6 (see, for example, So0 et al, 1960; Lee and Durst, 1982;Arnason and Stock, 1984;Tsuji et al, 1984). Mass loading is defined as the mass ratio of solids to gas, and values of 50 or higher are typically encountered in applications such as FCC risers.…”
Section: Dusty Gas Limitmentioning
confidence: 99%
“…It is less meaningful for turbulent shear flows, however, which is the case of turbulent pipe flow. A method is developed to allow local estimates for the diffusivity to be obtained when the turbulence is neither homogeneous nor isotropic [31]. If the flux is considered to be caused only by gradient diffusion (Fick's law), the particle dispersion coefficient at every radial location can be computed according to the following formula, except in regions where ∂C/∂r is near 0:…”
Section: Resultsmentioning
confidence: 99%
“…Chen and Crowe [74] simulated the experiment in a pipe flow of Arnason [75,76] and for the near isotropic homogeneous grid turbulence in Snyder and Lumley's experiments [15]; however they calibrated the model by changing the constant C µ to fit the last experiment. Durst et al [77] developed a simple EIM based on the previous work of Gosman and Ioannides [67,68], and the equation of motion was solved analytically for short time steps.…”
Section: Historical Backgroundmentioning
confidence: 99%
“…Durst et al [77] developed a simple EIM based on the previous work of Gosman and Ioannides [67,68], and the equation of motion was solved analytically for short time steps. Milojevic [78] optimized the model for various test flow configurations [15,16,75,76]. It was modified for particulate two-phase systems with a size distribution by Sommerfeld and coworkers [79,80].…”
Section: Historical Backgroundmentioning
confidence: 99%