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Journal ArticleDOI

A model for velocity and eddy diffusivity distributions in fully turbulent pipe flow

TLDR
In this paper, a model for the eddy diffusivity and mean velocity distributions in fully developed turbulent isothermal smooth pipe flow (4 x lo3 < Re < 5 x 10').
Abstract
A model was developed for the eddy diffusivity and mean velocity distributions in fully developed turbulent isothermal smooth pipe flow (4 x lo3 < Re < 5 x 10'). Reichardt's tworegion eddy diffusivity models were modified so as to fulfill the requirements that the eddy diffusivity be represented by a smooth, continuous curve, and vanish with the third power of the distance from the wall; the continuity equation be satisfied; and the ratio of the bulk velocity to centerline velocity agree with experimental data. The descripition is in excellent agreement with Laufer's experimental mean velocity data and, in general, provides a method of accurately predicting the mean velocity distribution. n turbulent flow, the instantaneous flow properties I are normally expressed as the sum of a time-averaged component and a fluctuating component. In an effort to provide engineering solutions to problems involving turbulent processes, which are difficult to describe on a mechanistic basis, the eddy diffusivity concept has been widely used to provide models for the fluctuating motion'". Unfortunately, the eddy diffusivity of momentum, a major parameter in most models, has not been well described in a manner consistent with the boundary conditions and available experimental data'a'. An objective of this work is, therefore, to generate an expression for the eddy diffusivity which will be compatible with both the boundary conditions and experimental data. A second concurrent objective is the development of a consistent expression for the mean velocity distribution. The approach used involves the iterative solution of mutually dependent expressions for the velocity distribution and eddy diffusivity in response to experimental and analytical constraints, in order to develop the most consistent over-all picture. Although an incompressible constant property fluid in fully-developed pipe flow is assumed in the model, such assumptions are often made in initial, idealized analyses of practical systems.

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Citations
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Journal ArticleDOI

The prediction of turbulent Prandtl and Schmidt numbers

TL;DR: In this article, more than thirty ways of predicting the relationship between turbulent transfers of momentum and a passive contaminant such as heat or dissolved matter are examined, divided into seven classes, on the basis of method of derivation or field of application.
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Turbulence-driven secondary flows and formation of sand ridges

TL;DR: In this paper, a linear stability analysis of flow in infinitely wide channels with an erodible bed is presented, and a nonlinear turbulence closure scheme is used to model the generation of turbulence-driven cellular secondary motions, eventually leading to the formation of sand ridges irrespective of the presence of the sidewalls.
Journal ArticleDOI

Measurements of the radial and tangential eddy diffusivities of heat and mass in turbulent flow in a plain tube

TL;DR: In this article, an experimental study was made of the variation of the radial and tangential eddy diffusivities of heat and mass in a fully developed turbulent flow in a plain tube.
Journal ArticleDOI

Eddy diffusivity of particles in turbulent flow in rough channels

TL;DR: In this paper, it is shown that the ratio of the eddy diffusion coefficient of particles to the fluid diffusion coefficient is dependent mainly on the friction velocity of fluid (U ∗ ), the sedimentation velocity of the particles (V s ), the Reynolds number (Re ) of the flow and also the relative roughness of channel ( e / D ).
Journal ArticleDOI

46 Two dimensional model for the simulation of tubular reactors for thermal cracking

TL;DR: In this article, the simulation of an industrial tubular reactor for the thermal cracking of ethane is based on a two-dimensional model consisting of a continuity equation for each component, an energy equation and a pressure drop equation.
References
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Journal ArticleDOI

On Turbulent Flow Near a Wall

TL;DR: In this paper, the authors defined the distance from wall pipe radius pipe diameter mean local velocity parallel to wall velocity fluctuations parallel and normal to flow mass density coefficient of viscosity shear stress velocity correlation coefficient mixing length universal constant in I = Ky modified universal constant eddy viscosities size of roughness friction factor = 8rw/p V 2
Journal ArticleDOI

Vollständige Darstellung der turbulenten Geschwindigkeitsverteilung in glatten Leitungen

TL;DR: From experimental investigations of turbulent exchange of momentum a formula is derived for the velocity of turbulent flow in tubes and pipes in this paper, which gives a complete representation of the velocity distribution, i. e. it holds good close to the wall as well as in the core of the flow.