Abstract
If a fluid enters an axially rotating pipe, it receives a tangential component of velocity from the moving wall, and the flow pattern change according to the rotational speed. A flow relaminarization is set up by an increase in the rotational speed of the pipe. It will be shown that the tangential- and the axial velocity distribution adopt a quite universal shape in the case of fully developed flow for a fixed value of a new defined rotation parameter. By taking into account the universal character of the velocity profiles, a formula is derived for describing the velocity distribution in an axially rotating pipe. The resulting velocity profiles are compared with measurements of Reich [10] and generally good agreement is found.
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Abbreviations
- b :
-
constant, equation (34)
- D :
-
pipe diameter
- l :
-
mixing length
- l 0 :
-
mixing length in a non-rotating pipe
- N :
-
rotation rate,N=Re ϕ /Re D
- p :
-
pressure
- R :
-
pipe radius
- Re D :
-
flow-rate Reynolds number,\(\operatorname{Re} _D = \bar v_z D/v\)
- Re ϕ :
-
rotational Reynolds number, Re ϕ =v ϕw D/ν
- Re*:
-
Reynolds number based on the friction velocity, Re*=v*R/ν
- (Re*)0 :
-
Reynolds number based on the friction velocity in a non-rotating pipe
- Ri:
-
Richardson number, equation (10)
- r :
-
coordinate in radial direction
- \(\tilde r\) :
-
dimensionless coordinate in radial direction,\(\tilde r = r/R\)
- v r ,v ϕ,v z :
-
time mean velocity components
- v′ r ,v′ ϕ ,v′ z :
-
velocity fluctations
- v ϕw :
-
tangential velocity of the pipe wall
- v*:
-
friction velocity,\(v_* = \sqrt {\left| {\tau _{rz} } \right|w/\rho } \)
- \(\bar v_z \) :
-
axial mean velocity
- v ZM :
-
maximum axial velocity
- \(\tilde y\) :
-
dimensionless radial distance from pipe wall,\(\tilde y = 1 - \tilde r\)
- y + :
-
dimensionless radial distance from pipe wall
- y +1 :
-
constant
- Z :
-
rotation parameter,Z =v ϕw/v * =N Re D /2Re*
- ε m :
-
eddy viscosity
- (ε m )0 :
-
eddy viscosity in a non-rotating pipe
- λ :
-
coefficient of friction loss
- κ :
-
von Karman constant
- κ 1 :
-
constant, equation (31)
- ρ :
-
density
- μ :
-
dynamic viscosity
- ν :
-
kinematic viscosity
References
Borisenko, A.I., Kostikov, O.N. and Chumachenko, V.I., Experimental study of turbulent flow in a rotating channel.J. Engng. Phys. 24 (1973) 770–773.
Hirai, S. and Takagi, T., Prediction of heat transfer deterioration in turbulent swirling pipe flow. In:Proc. 2nd ASME/JSME Thermal Engng. Joint Conf. 5 (1987) pp. 181–187.
von Kármán, T., Über laminare und turbulente Reibung.Z. Ang. Math. Mech. 1 (1921) 233–251.
Kikuyama, K., Murakami, M., Nishibori, K. and Maeda, K., Flow in an axially rotating pipe.Bull. JSME 26 (1983) 506–513.
Koosinlin, M.L., Launder, B.E. and Sharma, B.I., Prediction of momentum, heat and mass transfer in swirling, turbulent boundary layers.J. Heat Transfer 96 (1975) 204–209.
F. Levy, Strömungserscheinungen in rotierenden Rohren.VDI Forsch. Arb. Geb. Ing. Wes. 322 (1929) 18–45.
Murakami, M. and Kikuyama, K., Turbulent flow in axially rotating pipes.J. Fluids Engng. 102 (1980) 97–103.
Lord Rayleigh, On the dynamics of revolving fluids. In:Proc. R. Soc. A93 (1917) pp. 148–154.
Reichardt, H., Vollständige Darstellung der turbulenten Geschwindigkeitsverteilung in glatten Leitungen.Z. Ang. Math. Mech. 31 (1951) 208–219.
Reich, G. and Beer, H., Fluid flow and heat transfer in an axially rotating pipe — I. Effect of rotation on turbulent pipe flow.Int. J. Heat Mass Transfer 32 (1989) 551–562.
Schlichting, H., Grenzschicht-Theorie. Karlsruhe: G. Braun (1982).
Shchukin, V.K., Hydraulic resistance of rotating tubes.J. Engng. Phys. 12 (1967) 418–422.
Taylor, G.I., Stability of a viscous liquld contained between two rotating cylinders.Phil. Trans. R. Soc. London A223 (1923) 289–343.
Tietjens, O., Ströhmungslehre, Zweiter Band. Berlin/Heidelberg/New York: Springer (1970).
White, A., Flow of fluid in an axially rotating pipe.J. Mech. Engng. Sci. 6 (1964) 47–52.
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Weigand, B., Beer, H. On the universality of the velocity profiles of a turbulent flow in an axially rotating pipe. Appl. Sci. Res. 52, 115–132 (1994). https://doi.org/10.1007/BF00868054
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DOI: https://doi.org/10.1007/BF00868054