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Scale effects in polymer solution pipe flow

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Abstract

Satisfactory scaling from laboratory-scale pipe-flow data to large industrial pipelines is an area of practical concern in the utilization of drag-reducing polymer solutions. From experimental data for pipes 0.0254 m in diameter and above, it is shown that accurate scaling can be obtained using a simple, pocket-calculator method. However, pipes of say, 0.005 m and smaller provide much less accurate scaling data for larger pipes. A detailed study of the velocity profiles in drag-reducing flow indicates a total lack of similarity of the profiles of the very small pipes compared with the larger.

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Abbreviations

A,B :

constants in velocity profile equation

ΔB :

constant indicating drag reduction

D:

pipe diameter, m

k:

Karman constant (reciprocal of A)

k s :

height of sand-type roughness, m

N :

nondimensional negative roughness parameter

Re :

Reynolds number, UD/v

U :

average velocity in pipe, m/sec

u + :

local velocity in pipe, nondimensionalized with u *

u * :

friction velocity, m/sec

y :

radial distance from pipe wall, m

y + :

nondimensional distance from wall, yu * /v

λ :

Darcy friction factor

v :

kinematic viscosity, m2/sec

1:

experimental data

2:

predicted

References

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Hoyt, J.W., Sellin, R.H.J. Scale effects in polymer solution pipe flow. Experiments in Fluids 15, 70–74 (1993). https://doi.org/10.1007/BF00195598

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  • DOI: https://doi.org/10.1007/BF00195598

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