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Mathematical model of the entry length in the flow of suspensions of solid particles in a gas

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Abstract

A mathematical model consisting of equations of mass and momentum and for the velocity field has been used for computing the entry length of the flow of non-Newtonian fluids in laminar, transition and turbulent regions. Experimental data measured in a vertical flow of a suspension of solid particles in air have been used for verifying the predictions.

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Abbreviations

n :

flow index for laminar flow

Re :

Reynolds number defined for the flow of the carrier medium

q :

exponent for turbulent flow

\(\bar R_\delta \) :

ratio of core radius with a flat velocity profile to pipe radius

ū c :

ratio of the axial component of local velocity in the core to mean velocity

w :

mean flow velocity

\(\bar X\) :

ratio of axial distance from the pipe entrance to the pipe radius

\(\bar x_L \) :

ratio of the entrance length to the pipe radius

\(\dot X\) :

relative mass fraction of particles

\(\bar y\) :

ratio of the distance from the pipe wall to the pipe radius

λ :

coefficient of pressure loss due to friction

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Lodes, A., Mierka, O. & Mičák, J. Mathematical model of the entry length in the flow of suspensions of solid particles in a gas. Rheol Acta 24, 488–492 (1985). https://doi.org/10.1007/BF01462495

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  • DOI: https://doi.org/10.1007/BF01462495

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