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Volume Partly Filled Pipes

Reference data and engineering information about volume partly filled pipes for fluid mechanics applications.

volumepartlyfilledpipes

Overview

Engineering reference data for Volume Partly Filled Pipes in fluid mechanics.

Key Formulas

Reynolds Number

Re=ρvDμRe = \frac{\rho v D}{\mu}

Ratio of inertial to viscous forces — determines flow regime.

Bernoulli's Equation

P+12ρv2+ρgh=constP + \frac{1}{2}\rho v^2 + \rho g h = \text{const}

Conservation of energy for steady, inviscid, incompressible flow.

Continuity Equation

A1v1=A2v2A_1 v_1 = A_2 v_2

Conservation of mass for incompressible flow.

Darcy-Weisbach

ΔP=fLDρv22\Delta P = f \frac{L}{D} \frac{\rho v^2}{2}

Pressure drop due to friction in a pipe.

Variables

SymbolDescriptionUnit
ReReReynolds number
ρ\rhoFluid densitykg/m³
vvFlow velocitym/s
DDCharacteristic dimensionm
μ\muDynamic viscosityPa·s
PPPressurePa
ffDarcy friction factor

Liquid Volume Reference Table

The following table provides volume calculations for liquid in partly filled horizontal pipes and tanks, based on liquid level and pipe/tank diameter.

30 rows
Liquid volume (m³) in partly filled horizontal pipes/tanks for given liquid levels and diameters.
Liquid Level(m)
Diameter 0.3()
Diameter 0.4()
Diameter 0.5()
Diameter 0.6()
Diameter 0.7()
Diameter 0.8()
Diameter 0.9()
Diameter 1.0()
Diameter 1.2()
Diameter 1.4()
Diameter 1.6()
Diameter 1.8()
0.10.02060.02460.0280.0310.03370.03630.03860.04090.0450.04880.05230.0556
0.150.03530.0430.04950.05530.06050.06520.06970.07390.08160.08860.09520.101
0.20.05010.06280.07330.08250.09070.09830.1050.1120.1240.1350.1450.155
0.250.06290.08260.09820.1120.1230.1340.1440.1540.1710.1860.2010.214
0.30.07070.1010.1230.1410.1580.1720.1860.1980.2210.2420.2610.279
0.350.1170.1470.1710.1920.2110.2290.2450.2740.3010.3250.348
0.40.1260.1680.20.2270.2510.2730.2930.330.3630.3930.421
0.450.1860.2270.2610.2910.3180.3430.3870.4270.4640.497
0.50.1960.2520.2940.330.3630.3930.4460.4940.5370.577
0.550.2710.3240.3680.4070.4430.5060.5610.6120.659
0.60.2830.3510.4040.4510.4920.5650.630.6890.743
0.650.3730.4370.4920.540.6250.70.7670.828
0.70.4660.5310.5870.6320.7440.840.9251
0.750.490.5660.6320.6850.770.8460.915
0.80.5980.6740.7450.8570.9781.091.18
0.850.6220.7120.7710.911.051.161.27
0.90.7450.8010.961.111.241.36
0.951.011.181.321.451.54
11.051.241.41.551.63
1.051.091.31.471.621.72
1.11.351.551.721.8
1.151.41.621.81.89
1.21.451.691.962.05
1.251.491.752.042.12
1.31.521.812.122.2
1.351.872.22.27
1.41.922.272.33
1.452.392.44
1.52.442.49
1.552.52

Source: engineeringtoolbox.com

Table Usage Notes

  • Empty cells indicate that the liquid level exceeds the pipe diameter for that size (physically impossible).
  • The volumes represent the actual liquid volume, not the total tank volume.
  • These values assume a perfectly circular and horizontal pipe/tank cross-section.
  • For partially filled vertical pipes or tanks with different geometries, different formulas apply.

Interactive Charts

Horizontal pipe or cylinder tank - liquid volume partly filled

References