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Skin friction and heat transfer in turbulent flow of structurally viscous fluids

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Abstract

Relations which contain no new empirical turbulence constants are proposed for calculation of the resistance coefficient and the Nusselt number in turbulent flow of structurally viscous fluids.

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Abbreviations

τ :

shear stresses

ϕ :

fluidity of liquid

y:

distance from surface

v* :

dynamic viscosity

v :

kinematic viscosity

ρ :

density

w:

flow velocity of liquid

¯w:

mean mass flow velocity

η :

dimensionless coordinate

ζ:

resistance coefficient

R:

pipe radius

D:

pipe diameter

Θ:

coefficient of structural stability of liquid

sb:

dimensionless parameter

ξ=1-y/R:

dimensionless coordinate

(μT:

turbulent viscosity

0:

at τw=0

1:

at edge of viscous sublayer

w:

at tube wall

References

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Authors and Affiliations

  1. Siberian Division AS USSR, Thermophysics Institute, Novosibirsk

    E. M. Khabakhpasheva

Authors
  1. E. M. Khabakhpasheva
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Khabakhpasheva, E.M. Skin friction and heat transfer in turbulent flow of structurally viscous fluids. Journal of Engineering Physics 11, 73–75 (1966). https://doi.org/10.1007/BF00831255

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  • DOI: https://doi.org/10.1007/BF00831255

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