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Steam Pipe Drip Legs

Reference data and engineering information about steam pipe drip legs for fluid mechanics applications.

steampipedriplegs

Overview

Engineering reference data for Steam Pipe Drip Legs 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
5 rows
Recommended dimensions for steam pipe drip legs (pockets).
Main Diameter(mm)
Main Diameter(in)
Pocket Diameter(mm)
Pocket Diameter(in)
Pocket Depth(mm)
Pocket Depth(in)
50250270028
80380370028
1004100470028
25010150670028
500202501070028

Source: engineeringtoolbox.com

Example: For an 80 mm (3 in) steam pipe, the recommended drip leg pocket diameter is 80 mm (3 in) with a pocket depth of 700 mm (28 in).

Drip Leg Placement Guidelines

Steam traps and drip legs should be installed at the following locations to ensure proper condensate removal:

  • On horizontal pipes, every 30 to 50 m (100 to 150 ft).
  • In front of pressure reducing valves to protect the equipment from condensate damage.
  • In front of control valves to prevent damage from condensate accumulation.
  • In front of normally closed valves to avoid condensate buildup that could damage the system upon valve opening.
  • At the bottom of vertical risers to collect condensate flowing downward.
  • At the end of steam mains (dead ends) to drain condensate from the line.

Interactive Charts

Steam pipe line - drip leg for condensate

References