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Journal ArticleDOI

Particle—gas dispersion effects in a round jet

TLDR
The fully developed region for a two-phase jet exhibits similarity for velocity and concentration as mentioned in this paper, where a power law expression approximates the velocity distribution and the square root of this profile coincides with the concentration distribution.
Abstract
The fully developed region for a two-phase jet exhibits similarity for velocity and concentration. A power law expression approximates the velocity distribution and the square root of this profile coincides with the concentration distribution. Measurements show that particle dispersion decreases with increase in particle concentration and the gas mixing rate is lower than the particle mixing rate. The turbulent Schmidt Number remains constant at a value equal to 0.47. La region de l'ecoulement pleinement developpe pour un jet a deux phases presente une similitude pour la vitesse et la concentration. Une loi puissance donne une approximation de la distribution des vitesses et la racine carree de ce profil coincide avec la distribution de la concentration. Les mesures obtenues indiquent que la dispersion des particules decroit lorsque la concentration des particules augmente et que la vitesse de melange du gaz est plus petite que celle des particules. Le nombre de Schmidt de turbulence demeure constant a la valeur de 0.47.

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Citations
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Journal ArticleDOI

Particle mixing in free shear flows

TL;DR: In this article, the authors reviewed the currently accepted mechanisms and models for particle dispersion in homogenoue, isotropic turbulence and addressed the difference between such flows and free shear layers.
Journal ArticleDOI

A turbulence closure model for dilute gas-particle flows

TL;DR: In this article, a second order closure scheme is developed for the numerical prediction of isothermal, non-reacting, mono-dispersed, dilute gas-particle turbulent shear flows.
Journal ArticleDOI

Catalytic effect of lignite ash on steam gasification of oil sand coke

E. Furimsky, +1 more
- 16 Jun 1986 - 
TL;DR: In this paper, steam gasification of Suncor and Syncrude cokes was carried out in the presence of ash obtained after burning Onakawana lignite, and Catalytic effects of the ash were evident at 930°C whereas at 830°c little effect was observed.
Journal ArticleDOI

Modeling the mixing of a gas–liquid spray jet injected in a gas–solid fluidized bed: The effect of the draft tube

TL;DR: In this article, a two-dimensional model that characterizes the radial mixing by means of an eddy diffusivity coefficient is presented, and the model predictions are validated by experimentally measuring the liquid-solids mixing by a technique based on temperature measurements in the spray region.
Journal ArticleDOI

Particle concentration and size measurements in two-phase turbulent coaxial jets

TL;DR: In this article, particle concentration and particle size distributions have been measured for two-phase (solid/air) turbulent coaxial jets using the Laser Diffraction Method (LDM) and a tomography data transform technique.
References
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Journal ArticleDOI

A model of the two-phase turbulent jet

TL;DR: In this paper, a model of the two-phase turbulent jet is presented and a set of model differential equations is developed for cases in which the mean velocities of the phases are sensibly equal.
Journal ArticleDOI

Jet diffusion in the region of flow establishment

TL;DR: In this article, measurements were made of mean axial and radial velocities, mean static pressure, turbulence intensities, turbulent shear, and pressure fluctuation in the flow establishment region of an air jet issuing with an efflux velocity of about 35 ft/sec from a 1.0 ft. diameter nozzle into still air.
Journal ArticleDOI

Diffusion of Sediment in a Submerged Jet

TL;DR: The relationship between the ratio of the eddy diffusivity for sediment to the particle Reynolds number was obtained from the measured velocity and sediment-concentration distributions in a vertical, axi-symmetric, sediment-laden submerged jet directed downward into stationary water as mentioned in this paper.
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