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body | --uriencoded--f_%7BCW%7D(\mbox%7BRe%7D, \epsilon) |
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| Colebrook–White correlation |
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body | --uriencoded--\displaystyle k = \frac%7B f_%7BCW%7D( \mbox%7BRe%7D =4,000, \, \epsilon) -0.03048%7D%7B1,900%7D |
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| interpolation multiplier between laminar and turbulent flow regimes |
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| f = \frac{64}{\rm Re} \cdot \Phi |
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Chirchil[1+ left(\ / 812} }{Theta_1 + \Theta_2cdot \ln \frac{{\rm Re}}{5.37} \right)^{-2 \,(1 |
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.5} } -a)\,b}
\cdot \left( 0.83 \cdot \ln \frac{3.41}{\epsilon/d} \right |
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]1/12\Theta_1 2.457 \, \ln \left( 7}{\rm Re}}{2712} \right)^{ |
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09 + 0.27 \, \frac{epsilon}{d} \) \right16\Theta_2 = 37530}{\rm Re} \cdot \epsilon/d}{150} \right)^{1.8} \right]^{ |
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16
Cheng full-range model
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| f = \frac{64}{\rm Re} \cdot \Phi |
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| \Phi = \left( \frac{{\rm Re}}{64} \right)^{1-a}
\cdot \left( 1.8 \cdot \ln \frac{{\rm Re}}{6.8} \right)^{-2 \,(1-a)\,b}
\cdot \left( 2.0 \cdot \ln \frac{3.7}{\epsilon/d} \right)^{-2 \,(1-a)\,(1-b)} |
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| a = \left[ 1+ \left( \frac{{\rm Re}}{2720} \right)^9 \right]^{-1} |
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| b = \left[ 1+ \left( \frac{{\rm Re} \cdot \epsilon/d}{160} \right)^2 \right]^{-1} |
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LaTeX Math Block |
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| f = \frac{64}{\rm Re} \cdot \Phi |
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Cheng({}}{64}1-a}
\cdot 0.75cdot \ln \frac{{\rm Re}}{5.37}Theta_1 + \Theta_2 \right)^{ |
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-2 \,(1-a)\,b}
\cdot \left( 0.83 \cdot \ln \frac{3.41}{\epsilon/d} \right)^{-2 \,(1-a)\,(1-b)a1+ 2.457 \, \ln \left( \left( \frac{7}{\rm Re} \right)^{0.9} |
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{2712 + 0.27 \, \frac{\epsilon}{d} \right) |
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^8.4-1b[ 1+ \left(cdot \epsilon/d}{150} \^1.8 \right]-1
See also
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Physics / Fluid Dynamics / Pipe Flow Dynamics / Darcy–Weisbach equation / Darcy friction factor
[ Surface roughness ] [ Reduced Friction Factor (Φ) ]
Reference
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Moody’s Friction Factor Calculator @ gmallya.com
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