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