Conservation-Law Approach for Transition in Pipe Flows

The laminar to turbulent transition in a pipe flow is studied from the viewpoint of momentum conservation. The transition is presumed to happen downstream of the laminar flow development. The inflow conditions to the transition region are presumed not to change at the moment of transition. The exit pressure is presumed not to change either. In the present model, the turbulent transition is a function of the ratio of the pipe length to its diameter, and becomes larger as the pipe length ratio increases. The natural transition Reynolds number calculated shows reasonable agreement with previous experimental results. The critical transition Reynolds number calculated is 1,752, and is close to the critical number of 1,760 measured previously. The distribution of difference in pressure drop between the laminar and turbulent flows corresponds to the reported location of the puffs and slugs in the Reynolds number under forced transition.

[1]  B. Launder,et al.  Laminarization of the Turbulent Boundary Layer in a Severe Acceleration , 1964 .

[2]  F. Durst,et al.  Laminar-to-turbulent transition of pipe flows through puffs and slugs , 2008, Journal of Fluid Mechanics.

[3]  M. R. Head,et al.  Reversion of turbulent to laminar flow , 1968, Journal of Fluid Mechanics.

[4]  J. Westerweel,et al.  Experimental Observation of Nonlinear Traveling Waves in Turbulent Pipe Flow , 2004, Science.

[5]  F. Nieuwstadt,et al.  Laminar–turbulent transition in pipe flow for Newtonian and non-Newtonian fluids , 1998, Journal of Fluid Mechanics.

[6]  Antonio Delgado,et al.  Evolution of transitional structures from puff to slug through multiple splitting in a pipe flow at low Reynolds number , 2011 .

[7]  A. M. Binnie,et al.  A study by a double-refraction method of the development of turbulence in a long circular tube , 1947, Proceedings of the Royal Society of London. Series A. Mathematical and Physical Sciences.

[8]  I. Wygnanski,et al.  On transition in a pipe. Part 1. The origin of puffs and slugs and the flow in a turbulent slug , 1973, Journal of Fluid Mechanics.

[9]  F. Durst,et al.  The Development Lengths of Laminar Pipe and Channel Flows , 2005 .

[10]  B. Hof Transition to Turbulence in Pipe Flow , 2022, Annual Review of Fluid Mechanics.

[11]  A. Smits,et al.  Mean-flow scaling of turbulent pipe flow , 1998, Journal of Fluid Mechanics.

[12]  T Mullin,et al.  Decay of turbulence in pipe flow. , 2006, Physical review letters.

[13]  M. R. Head,et al.  Some observations on skin friction and velocity profiles in fully developed pipe and channel flows , 1969, Journal of Fluid Mechanics.

[14]  Jerry Westerweel,et al.  Turbulence transition in pipe flow , 2007 .

[15]  Franz Durst,et al.  Forced laminar-to-turbulent transition of pipe flows , 2006, Journal of Fluid Mechanics.

[16]  T. Kanda Conservation-Law Approach to Prediction of Boundary Layer Transition , 2011 .

[17]  A Conservation-Law Approach to Predicting the Length of the Boundary Layer Transition Region , 2012 .

[18]  T. Mullin,et al.  Transition to turbulence in constant-mass-flux pipe flow , 1995, Journal of Fluid Mechanics.

[19]  T. Mullin,et al.  Experimental and theoretical progress in pipe flow transition , 2008, Philosophical Transactions of the Royal Society A: Mathematical, Physical and Engineering Sciences.

[20]  R. Kerswell,et al.  Recent progress in understanding the transition to turbulence in a pipe , 2005 .

[21]  T. Mullin,et al.  Finite-amplitude thresholds for transition in pipe flow , 2007, Journal of Fluid Mechanics.

[22]  F. White Viscous Fluid Flow , 1974 .