Pressure loss of the viscous flow through straight pipes
dimensioned variables (metric as example) |
Δ p | [kg/(m s²) = 10-5 bar = 10-2mbar] | : Pressure loss of the straight pipe |
l | [m] | : Length |
d | [m] | : Internal Diameter |
ρ | [kg/m³] | : Density |
v | [m/s] | : Average speed in the pipe |
η | [kg/(m s) = Pas] | : Dyn. Viscosity |
ε | [m] | : Roughness |
dimensionless values |
Re | [-] | : Reynolds number Re = ρ v d / η |
f | [-] |
: Darcy Friction Factor |
For Re < 2320 (laminar flow) the Darcy Friction Factor is calculated according to Hagen-Poiseuille:
f = 64 / Re
Hagen Poiseuille and Couette Flow
For Re > 2320 (turbulent flow) the Darcy Friction Factor is calculated according to [Colebrook 1939, page 137]:
For Re => ∞ (completely turbulent flow) the equation of Colebrook converges to the
equation of [Prandtl 1933, page 110] according to Kármán:
and for ε/d => 0 (smooth pipe) to the equation of [Prandtl 1933, page 111]:
Laminar flow is possible for Re < 8000 [VDI 1984, page Lb1]. In the critical transition
zone (2320 <= Re < 8000) the value of the Darcy Friction Factor might be overestimated
by the means of calculation presented above.
The Moody-diagram [Moody 1944, page 672] is a successful illustration of the equations
presented above.
| |
|
Moody Re: 10-106 | |
Moody Re: 100-108 |
With 1/f^0,5 = Re/200 · ε /d and
1/f^0,5 = 2log(r/ε) + 1,74 [Moody 1944, page 676] draws a line between
the transition zone and the completely turbulent pipe flow.
Literature
|
[Colebrook 1939] C.F. Colebrook, Turbulent Flow in Pipes,
with particular reference to the Transition Region between the Smooth and Rough
Pipe Laws, Journal of The Institution of Civil Engineers, Volume 11, 1939 |
[Moody 1944] L.F.Moody, Friction Factors of Pipe Flow,
Transactions of the ASME, Volume 66, 1944 |
[Prandtl 1933] L. Prandtl, Neuere Ergebnisse der
Turbulenzforschung, Zeitschrift des Vereins Deutscher Ingenieure, Band 77, 1933 |
[VDI 1984] VDI-Wärmeatlas 4. Auflage 1984 |