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Granular Flow and Rheology Under Shear, Vibration and Gas Flow.
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Granular Flow and Rheology Under Shear, Vibration and Gas Flow.
자료유형  
 학위논문
Control Number  
0017164610
International Standard Book Number  
9798342112697
Dewey Decimal Classification Number  
660
Main Entry-Personal Name  
Sanghishetty, Jagan Mohan.
Publication, Distribution, etc. (Imprint  
[S.l.] : Columbia University., 2024
Publication, Distribution, etc. (Imprint  
Ann Arbor : ProQuest Dissertations & Theses, 2024
Physical Description  
97 p.
General Note  
Source: Dissertations Abstracts International, Volume: 86-04, Section: B.
General Note  
Advisor: Boyce, Christopher M.
Dissertation Note  
Thesis (Ph.D.)--Columbia University, 2024.
Summary, Etc.  
요약Granular flows are ubiquitous both in natural and industrial processes such as pharmaceuticals production, mining and food-processing. Within a gas-solid fluidized bed, fundamental phenomena such as heat and mass transfer are impacted by particle convection, mixing and segregation due to rising gas bubbles. The free-bubbling regime is promising in enhancing the gas-solid contact but its mathematically chaotic bubble motion make system design challenging. Furthermore, a better understanding of rheological characteristics of these gas-solid flows is pertinent to developing accurate mathematical descriptions of granular flows. Despite their decades of usage and significance in all walks of technology, gas-solid fluidized beds remain poorly understood.In the first section of this dissertation, we investigate the combined effects of vibration and gas flow on a binary gas-solid fluidized bed. At resonant conditions, this external excitation generates a periodic, triangular, equisized, structured array of rising bubbles, reducing the chaos. Through a combination of experiments, Computational Fluid Dynamics-Discrete Element Method (CFD-DEM), and Multi Fluid Model (MFM) simulations, we demonstrate that the structured bubbling facilitates particle mixing whereas the gas flow alone (no vibration conditions) results in smaller, unstructured bubbles that promote segregation. The CFD-DEM simulations accurately capture the bubble structuring and somewhat, qualitatively and quantitively, match with the optically imaged experimental data. These investigations provide valuable insights into the dynamics of particle mixing and segregation under complex fluidization conditions. The MFM simulations failed to predict the mixing observed, indicating a need for further refinement of these models.In the second section of this dissertation, we explore the complex rheological behavior of the dry, dense particulate flows using the Discrete Element Method (DEM) simulations. In these simulations, we choose 3−D Couette cell geometry to visualize Granular Taylor-Vortex flow for various particle diameters and densities. The simulations examined the effects of varying particle volume fractions, from 0.45 to 0.60, under different shear rates, revealing a distinct rheological transition from shear-thickening to Newtonian and finally to shear-thinning behavior. The formation and nature of these vortices were compared with those observed in continuum simulations of Newtonian and shear-thinning fluids, to elucidate the unique aspects of granular flow dynamics.The third section of this thesis investigated the rheology of granular particles subjected to 1−D shear combined with sinusoidal vibration, aiming to understand the effects on pressure, shear stress, and coordination number across a range of shear rates and particle fractions. A novel vibrational regime was observed at low shear rates, below a critical threshold, characterized by a rate-independent pressure intermediate between the inertial and quasi-static regimes. These findings provide significant insights while advancing our understanding of granular material dynamics.
Subject Added Entry-Topical Term  
Chemical engineering.
Subject Added Entry-Topical Term  
Physics.
Subject Added Entry-Topical Term  
Physical chemistry.
Index Term-Uncontrolled  
Computational Fluid Dynamics
Index Term-Uncontrolled  
Discrete Element Method
Index Term-Uncontrolled  
Fluidization
Index Term-Uncontrolled  
Granular flows
Index Term-Uncontrolled  
Rheology
Added Entry-Corporate Name  
Columbia University Chemical Engineering
Host Item Entry  
Dissertations Abstracts International. 86-04B.
Electronic Location and Access  
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Control Number  
joongbu:656575
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