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Behavior of dispersed particles in turbulent liquid flow

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TLDR
In this paper, the effects of these scales on the magnitude of turbulence velocity components are examined, and the magnitudes are evaluated with a set of values of scales which seem most appropriate to each particle motion.
Abstract
Turbulent motion of particles suspended in water in a stirred tank and that of drops supplied to turbulent pipe flow of water are studied with emphasis on their scales. The scales considered are 1) sampling time scale : the very small time interval in which the displacement of a particle is measured, 2) measuring time scale : the time-duration during which a continuous measurement is run, and 3) sampling spatial scale : the width of a location in which the displacement of a particle is followed. The effects of these scales on the magnitude of turbulence velocity components are examined, and the magnitudes are evaluated with a set of values of scales which seem most appropriate to each particle motion. The magnitudes are correlated uniformly in both dispersions with particle diameters and energy dissipation rates of surrounding liquid.

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Journal ArticleDOI

Modeling of Bubble Column Reactors: Progress and Limitations

TL;DR: In this article, the progress reported in the literature during the past decade regarding the use of averaged Eulerian multifluid models and computational fluid dynamics (CFD) to model vertical bubble-driven flows is reviewed.
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Mass transfer to microparticles in agitated systems

TL;DR: In this article, the theoretical limit of Sherwood number 2 for spherical particles suspended in stirred tanks was confirmed, which is the first systematic experimental confirmation that the theory is valid for spherical particle suspensions.
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Population Balance Modeling of Aerated Stirred Vessels Based on CFD

TL;DR: In this paper, the authors used population balance equations (PBE) to predict local gas fraction and bubble-size distributions for turbulent gas dispersion in a stirred vessel, with relations taken from literature for bubble coalescence and breakup derived from isotropic turbulence theory.
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Modelling asphaltene deposition in turbulent pipeline flows

TL;DR: In this paper, an asphaltene deposition model in a pipeline is presented based on data obtained by experiments performed in a Couette device, where the inner cylinder rotates, and deposition on the outer wall is studied.
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Phenomenological model for bubble column reactors: prediction of gas hold-ups and volumetric mass transfer coefficients

TL;DR: Based on a phenomenological model for bubble break-up and coalescence, a new simulation model for gas holdup and gas-liquid mass transfer in bubble column reactors is proposed in this article.
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