Drop Coalescence in Turbulent Liquid-liquid Dispersions PDF Download

Author: Ramachandran Muralidhar
Publisher:
ISBN:
Category : Agglomeration
Languages : en
Pages : 516

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Author: Michael A. Delichatsios
Publisher:
ISBN:
Category :
Languages : en
Pages : 5

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Author: C.G. Vindon (Jr.)
Publisher:
ISBN:
Category :
Languages : en
Pages :

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Author: Wioletta Podgórska
Publisher: CRC Press
ISBN: 1482235706
Category : Science
Languages : en
Pages : 482

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Multiphase Particulate Systems in Turbulent Flows: Fluid-Liquid and Solid-Liquid Dispersions provides methods necessary to analyze complex particulate systems and related phenomena including physical, chemical and mathematical description of fundamental processes influencing crystal size and shape, suspension rheology, interfacial area of drops and bubbles in extractors and bubble columns. Examples of mathematical model formulation for different processes taking place in such systems is shown. Discussing connections between turbulent mixing mechanisms and precipitation, it discusses influence of fine-scale structure of turbulence, including its intermittent character, on breakage of drops, bubbles, cells, plant cell aggregates. An important aspect of the mathematical modeling presented in the book is multi-fractal, taking into account the influence of internal intermittency on different phenomena. Key Features Provides detailed descriptions of dispersion processes in turbulent flow, interactions between dispersed entities, and continuous phase in a single volume Includes simulation models and validation experiments for liquid-liquid, gas-liquid, and solid-liquid dispersions in turbulent flows Helps reader learn formulation of mathematical models of breakage or aggregation processes using multifractal theory Explains how to solve different forms of population balance equations Presents a combination of theoretical and engineering approaches to particulate systems along with discussion of related diversity, with exercises and case studies

Author: Wioletta Podgórska
Publisher: CRC Press
ISBN: 1351644653
Category : Science
Languages : en
Pages : 384

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Book Description
Multiphase Particulate Systems in Turbulent Flows: Fluid-Liquid and Solid-Liquid Dispersions provides methods necessary to analyze complex particulate systems and related phenomena including physical, chemical and mathematical description of fundamental processes influencing crystal size and shape, suspension rheology, interfacial area of drops and bubbles in extractors and bubble columns. Examples of mathematical model formulation for different processes taking place in such systems is shown. Discussing connections between turbulent mixing mechanisms and precipitation, it discusses influence of fine-scale structure of turbulence, including its intermittent character, on breakage of drops, bubbles, cells, plant cell aggregates. An important aspect of the mathematical modeling presented in the book is multi-fractal, taking into account the influence of internal intermittency on different phenomena. Key Features Provides detailed descriptions of dispersion processes in turbulent flow, interactions between dispersed entities, and continuous phase in a single volume Includes simulation models and validation experiments for liquid-liquid, gas-liquid, and solid-liquid dispersions in turbulent flows Helps reader learn formulation of mathematical models of breakage or aggregation processes using multifractal theory Explains how to solve different forms of population balance equations Presents a combination of theoretical and engineering approaches to particulate systems along with discussion of related diversity, with exercises and case studies

Author: Thomas Grove Tobin
Publisher:
ISBN:
Category : Agglomeration
Languages : en
Pages : 314

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Author: Jin Yong Park
Publisher:
ISBN:
Category : Mixing
Languages : en
Pages : 126

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Author: Laurence R. Weatherley
Publisher: Cambridge University Press
ISBN: 1108421016
Category : Mathematics
Languages : en
Pages : 379

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Explore and review novel techniques for intensifying transport and reaction in liquid-liquid and related systems with this essential toolkit. Topics include discussion of the principles of process intensification, the nexus between process intensification and sustainable engineering, and the fundamentals of liquid-liquid contacting, from an expert with over forty-five years' experience in the field. Providing promising directions for investment and for new research in process intensification, in addition to a unique review of the fundamentals of the topic, this book is the perfect guide for senior undergraduate students, graduate students, developers, and research staff in chemical engineering and biochemical engineering.

Author: Thomas G. Tobin
Publisher:
ISBN:
Category :
Languages : en
Pages : 314

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Author: John Philip Ward
Publisher:
ISBN:
Category : Fluid dynamics
Languages : en
Pages : 706

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The momentum transfer characteristics of liquid-liquid dispersions were studied under conditions of turbulent flow in a cirular conduit. Experiments were conducted to obtain drop size, friction factors and velocity profiles for three organic phases dispersed in water. The test sections consisted of straight copper tubes 1-inch OD and 0.830-inch ID. The velocity profiles and drop size measurements were made at a point 8-1/2 feet downstream from the entrance to these tubes. The dispersions were formed and maintained by the mixing action of a high speed centrifugal pump. The organic phases were a light petroleum solvent, a light oil and a heavy oil with viscosities of 1, 15, and 200 centipoise, respectively. Flow rates were in the range 1-4 lb/sec and concentrations from 5 to 50 volume percent were studied. A photographic method of drop size determination was developed. Excellent results are obtained for drop diameters in the range 5-800 microns. Dispersions with concentrations from 1 to 50 volume percent were photographed. The drop size and the shape of the drop size distributions depended strongly on dispersed phase viscosity. The range of drop diameters was found to increase with dispersed phase viscosity. Velocity profile data were obtained in the turbulent core for three flow rates and four concentrations for the light oil dispersions and two flow rates and three concentrations for the heavy oil dispersions. The light oil dispersions were found to behave as single phase Newtonian fluids. The solvent dispersions have previously been shown to behave as single phase Newtonian liquids. The heavy oil dispersions did not behave as Newtonian fluids. These results were combined with the drop size data and a previously proposed criteria for treating dispersions as single phase fluids to give the relation [see PDF for formula] where d32 is the Sauter mean diameter of the dispersed drops. Dispersions which do not meet this criterion are presumed to have a "slip" velocity, i.e., the larger drops move relative to the fluid element in which they are contained. Thus they do not behave as a single phase fluid. The velocity profiles for the light oil dispersions were used to calculate an effective dispersion viscosity [mu subscript e]. The viscosity increased with dispersed phase concentration. Effective viscosities for the solvent dispersion had been determined by previous workers. A comparison of the viscosities and drop size data for these two systems shows that at equal concentrations the effective viscosity of a dispersion is a function of the drop size distribution, decreasing with increasing size range. Effective viscosities for the heavy oil dispersions were determined from the friction factor data and appeared to be independent of concentration in the range 5 to 17 volume percent. This may be explained by a "slip" velocity and an analysis of the drop size distributions. A study was made of one water-in-solvent dispersion and it was found that water droplets adhered to the pipe wall. The average size of these droplets could be determined from the observed friction factor data. The droplets adhering to the wall were observed to undergo coalescence with the droplets in the flowing dispersion. Several other observations made through the optical portion of the photographic arrangement tend to support the coalescence theory recently proposed by Howarth.