Abstract
Results from a series of Theological and pipe flow experiments using watersoluble hydroxyethylcellulose and polyethyleneoxide are presented. Phenomena of drag reduction were investigated for values of concentration (in weight) of polymers in water ranging x = 10-4 to x = 5 · 10-3. Velocity measurements by using a laser-Doppler anemometer to type DISA-Mark II served for determining the variation in thickness of the elastic sublayer in the turbulent flow exhibiting drag reduction.
Similar content being viewed by others
Abbreviations
- A :
-
coefficient in Eq. (1)
- B :
-
coefficient in Eq. (1)
- D :
-
pipe diameter
- D:
-
shear velocity
- K :
-
consistency parameter in Eq. (5)
- n :
-
flow index of non-newtonian fluids
- r :
-
radial distance from the pipe center
- Re :
-
Reynolds number
- R :
-
pipe radius
- y :
-
distance from the pipe wall
- y + :
-
dimensionless distance from the pipe wall, (R-r)u * ϱ/μ
- y e + :
-
experimental value of the dimensionless thickness of the viscous and elastic sublayer
- y s + :
-
dimensionless thickness of the viscous and the elastic sublayer
- u + :
-
dimensionless local velocity, ΰ/*
- u * :
-
dynamic friction velocity, w(λ/8) o.5
- ΰ :
-
time-averaged local instantaneous velocity of flow
- w :
-
average velocity over the cross-section of the pipe
- X :
-
weight fraction of polymer in water solution
- μ :
-
viscosity
- λ :
-
fraction factor
- ϱ :
-
density
- v :
-
kinematic viscosity
- τ :
-
shear stress
References
Brodkey, R. S. 1967: The phenomena of fluid motions, p. 251. Massachusetts: Addison — Wesley P.C.
Berman, N. S. 1978: Drag reduction of polymers. Annu. Rev. Fluid Mech. 10, 47–64
Kowase, Y.; Ulbrecht, J. J. 1983: Turbulent heat and mass transfer in non-newtonian pipe flow: A model based on the surface renewal concept. Int. J. Phys. Chem. Hydrodyn. 4, 351–388 (Special issue 4th int. conf. physiochem. hydrodynamics)
Lodes, A. 1980: Stochastic and erodic properties of laser-Doppler signal sets averaging by the Pearson distribution. Proc. 6th symp. LDA. Bratislava: CHTF 382–01, pp. 79–96
Lodes, A.; Lodesová, D. 1986: Inner structure of turbulent drag reduction flow. Proc. 5th YAI ehem. eng. conf., Portorož, CSSR, pp. 131–138
Lodes, A.; Zaliberová, A.; Hudáčková, H. 1981: The influence of polymer additive on velocity distribution in the transition region of flow. Proc. conf. rheology of fluids in industrial praxis, Velké Karlovice, CSSR, pp. 177–182
Lodes, A.; Dúbrava, L.; Zaliberová, A. 1982: Determination of turbulent characteristics from the LDA data with noisy signals. Proc. 7th symp. LDA. Bratislava: CHTF 382–02, pp. 31–38
Lumley, J. L. 1969: Drag reduction by additives. Annu. Rev. Fluid Mech. 1, 367–383
Lumley, J. L. 1977: Drag reduction in the two phase and polymer flows. Phys. Fluids 20, 64–71
Mizushina, T.; Usui, H. 1977: Reduction of eddy diffusion for momentum and heat in viscoelastic fluid flow in a circular tube. Phys. Fluids. 20, 100–108
Pollert, J. 1986: Today and future possibilities of industrial applications of drag reduction. In: The influence of polymer additives on velcoity and temperature fields (ed. Gampert, B.), pp. 371–395. Proc. IUTAM-symp., Essen, FRG, 1984. Berlin, Heidelberg, New York: Springer
Schowalter, W. R. 1978: Mechanics of non-newtonian fluids, p. 244. Oxford: Pergamon Press
Sedov, L. I.; Iosolevich, V. A.; Pilipenko, V. N.; Vasetskaya, N. G. 1979: Turbulent diffusion and degradation of polymer molecules in a pipe and boundary layer. J. Fluid Mech. 94, 561–576
Virk, P. S. 1971: An elastic sublayer model for drag reduction by dilute solutions of linear macromolecules. J. Fluid Mech. 45, 417–437
Virk, P. S. 1975: Drag reduction fundamentals. AIChE J. 21, 625–656
Author information
Authors and Affiliations
Rights and permissions
About this article
Cite this article
Lodesová, D., Lodes, A. Thickness of the elastic sublayer in the velocity field of diluted polymeric solutions. Experiments in Fluids 7, 379–382 (1989). https://doi.org/10.1007/BF00193418
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF00193418