A new approach to understanding and modelling the influence of wall roughness on friction factors for pipe and channel flows

In this study, it is shown how the equivalent sand roughness required in the Moody chart can be calculated for arbitrarily shaped wall roughnesses. After a discussion of how to define the wall location and roughness height in the most reasonable way, a numerical approach based on the determination of entropy production in rough pipes and channels is presented. As test cases, three different two-dimensional roughness types have been chosen which are representative of regular roughnesses on machined surfaces. In the turbulent range, skin friction results with these test roughnesses can be linked to Nikuradse's sand roughness results by a constant factor. For laminar flows, a significant effect of wall roughness is identified which in most other studies is neglected completely. The dissipation model of this study is validated with experimental data for laminar and turbulent flows.

[1]  J. Nikuradse,et al.  Untersuchungen über turbulente Strömungen in nicht kreisförmigen Rohren , 1930 .

[2]  Flow Experiments With High Pressure Natural Gas In Coated And Plain Pipes: Comparison Of Transport Capacity , 1998 .

[3]  John Kim,et al.  Rough-Wall Turbulent Boundary Layers , 2004 .

[4]  S. Orszag,et al.  Renormalization group analysis of turbulence. I. Basic theory , 1986 .

[5]  C F Colebrook,et al.  TURBULENT FLOW IN PIPES, WITH PARTICULAR REFERENCE TO THE TRANSITION REGION BETWEEN THE SMOOTH AND ROUGH PIPE LAWS. , 1939 .

[6]  H. Herwig,et al.  Direct and indirect methods of calculating entropy generation rates in turbulent convective heat transfer problems , 2006 .

[7]  L. Schiller,et al.  Über den Strömungswiderstand von Rohren verschiedenen Querschnitts und Rauhigkeitsgrades , 1923 .

[8]  H. Herwig,et al.  Local entropy production in turbulent shear flows: a high-Reynolds number model with wall functions , 2004 .

[9]  J. Dittmer,et al.  A Systematic Approach to Wall Roughness Effects in Laminar Channel Flows: Experiments and Modelling , 2008 .

[10]  Dongqing Li,et al.  Influence of the three-dimensional heterogeneous roughness on electrokinetic transport in microchannels. , 2004, Journal of colloid and interface science.

[11]  S. Kandlikar,et al.  Characterization of surface roughness effects on pressure drop in single-phase flow in minichannels , 2005 .

[12]  Julian F. Scott,et al.  An Introduction to Turbulent Flow , 2000 .

[13]  J. E. Hesselgreaves Rationalisation of second law analysis of heat exchangers , 2000 .

[14]  Leslie M. Smith,et al.  Renormalization group analysis of turbulence , 2003 .

[15]  Zhen-Xiang Gong,et al.  Entropy Generation Minimization , 1996 .

[16]  A. Smits,et al.  Flow in a commercial steel pipe , 2008, Journal of Fluid Mechanics.

[17]  J. Koo,et al.  Computational Analysis of Wall Roughness Effects for Liquid Flow in Micro-Conduits , 2004 .

[18]  Peter Bradshaw A note on “critical roughness height” and “transitional roughness” , 2000 .

[19]  H. Schlichting Boundary Layer Theory , 1955 .

[20]  Victor L. Streeter,et al.  Frictional Resistance in Artificially Roughened Pipes , 1936 .

[21]  J. Nikuradse Stromungsgesetze in rauhen Rohren , 1933 .

[22]  G. Croce,et al.  Numerical simulation of roughness effect on microchannel heat transfer and pressure drop in laminar flow , 2005 .

[23]  Marc A. Rosen,et al.  Second‐law analysis: approaches and implications , 1999 .

[24]  B. Hua,et al.  Exergy destruction due to mean flow and fluctuating motion in incompressible turbulent flows through a tube , 2003 .

[25]  T. Papanastasiou,et al.  Viscous Fluid Flow , 1999 .

[26]  A. Smits,et al.  Roughness effects in turbulent pipe flow , 2006, Journal of Fluid Mechanics.