Turbulent Flow Friction Factor Calculation Using a Mathematically Exact Alternative to the Colebrook–White Equation

We present a novel, mathematically equivalent representation of the Colebrook–White equation to compute friction factor for turbulent flow in rough pipes. This new form is simple, no iterative calculations are necessary, and is well suited for accurate friction factor estimation. A limiting case of...

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Published in:Journal of hydraulic engineering (New York, N.Y.) Vol. 132; no. 8; pp. 863 - 867
Main Authors: Sonnad, Jagadeesh R, Goudar, Chetan T
Format: Journal Article
Language:English
Published: Reston, VA American Society of Civil Engineers 01-08-2006
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Abstract We present a novel, mathematically equivalent representation of the Colebrook–White equation to compute friction factor for turbulent flow in rough pipes. This new form is simple, no iterative calculations are necessary, and is well suited for accurate friction factor estimation. A limiting case of this equation provided friction factor estimates with a maximum absolute error of 0.029 and a maximum percentage error of 1% over a 20×500 grid of ε∕D and R values ( 10−6 ⩽ε∕D⩽5× 10−2 ; 4× 103 <R< 108 ). This was more accurate than the best currently available noniterative approximation of the Colebrook–White equation (maximum absolute error of 0.058; maximum percentage error of 1.42%). The superior accuracy, however, was obtained at the expense of a 30% increase in computational effort over the noniterative approximation. The novel equation presented in this study is theoretical and eliminates the need for best fit parameters or complicated initial guesses that are a characteristic of various empirical approximations proposed to date. The simplicity with which this new equation can be solved, coupled with its smooth and predictable error behavior, should make it the method of choice for estimating turbulent flow friction factor in rough pipes.
AbstractList We present a novel, mathematically equivalent representation of the Colebrook-White equation to compute friction factor for turbulent flow in rough pipes. This new form is simple, no iterative calculations are necessary, and is well suited for accurate friction factor estimation. A limiting case of this equation provided friction factor estimates with a maximum absolute error of 0.029 and a maximum percentage error of 1% over a 20 x 500 grid of epsilon /D and R values (10 super(-6) less than or equal to epsilon /D less than or equal to 5 x 10 super(-2); 4 x 10 super(3) < R < 10 super(8)). This was more accurate than the best currently available noniterative approximation of the Colebrook-White equation (maximum absolute error of 0.058; maximum percentage error of 1.42%). The superior accuracy, however, was obtained at the expense of a 30% increase in computational effort over the noniterative approximation. The novel equation presented in this study is theoretical and eliminates the need for best fit parameters or complicated initial guesses that are a characteristic of various empirical approximations proposed to date. The simplicity with which this new equation can be solved, coupled with its smooth and predictable error behavior, should make it the method of choice for estimating turbulent flow friction factor in rough pipes.
We present a novel, mathematically equivalent representation of the Colebrook–White equation to compute friction factor for turbulent flow in rough pipes. This new form is simple, no iterative calculations are necessary, and is well suited for accurate friction factor estimation. A limiting case of this equation provided friction factor estimates with a maximum absolute error of 0.029 and a maximum percentage error of 1% over a 20×500 grid of ε∕D and R values ( 10−6 ⩽ε∕D⩽5× 10−2 ; 4× 103 <R< 108 ). This was more accurate than the best currently available noniterative approximation of the Colebrook–White equation (maximum absolute error of 0.058; maximum percentage error of 1.42%). The superior accuracy, however, was obtained at the expense of a 30% increase in computational effort over the noniterative approximation. The novel equation presented in this study is theoretical and eliminates the need for best fit parameters or complicated initial guesses that are a characteristic of various empirical approximations proposed to date. The simplicity with which this new equation can be solved, coupled with its smooth and predictable error behavior, should make it the method of choice for estimating turbulent flow friction factor in rough pipes.
Author Goudar, Chetan T
Sonnad, Jagadeesh R
Author_xml – sequence: 1
  givenname: Jagadeesh R
  surname: Sonnad
  fullname: Sonnad, Jagadeesh R
  organization: Univ. of Oklahoma Health Sciences Center , Dept. of Radiological Sciences, , Oklahoma City, OK 73190
– sequence: 2
  givenname: Chetan T
  surname: Goudar
  fullname: Goudar, Chetan T
  email: chetan.goudar.b@bayer.com
  organization: Bayer HealthCare , Research and Development, Process Sciences, , Biological Products Division, 800 Dwight Way, Berkeley, CA 94710 (corresponding author). E-mail
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Issue 8
Keywords Fluid mechanics
Turbulent flow
Pipe flow
Friction
Hydraulics
Computation
Formulation
Fluid flow
Theoretical study
Mathematics
Mathematical model
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Snippet We present a novel, mathematically equivalent representation of the Colebrook–White equation to compute friction factor for turbulent flow in rough pipes. This...
We present a novel, mathematically equivalent representation of the Colebrook-White equation to compute friction factor for turbulent flow in rough pipes. This...
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SubjectTerms Applied sciences
Buildings. Public works
Computation methods. Tables. Charts
Exact sciences and technology
Hydraulic constructions
Piping
Structural analysis. Stresses
TECHNICAL NOTES
Water supply. Pipings. Water treatment
Title Turbulent Flow Friction Factor Calculation Using a Mathematically Exact Alternative to the Colebrook–White Equation
URI http://ascelibrary.org/doi/abs/10.1061/(ASCE)0733-9429(2006)132:8(863)
https://search.proquest.com/docview/19348033
Volume 132
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