Line Sizing Calculator

Calculate pressure drop and head loss for pipe systems with up to 3 pipe sections. Uses Darcy-Weisbach equation with Moody friction factor.

Incompressible Line Sizing Calculator Guide (PDF)

This calculator determines the pressure drop through a pipeline. It is suitable for incompressible flow. Incompressible flow refers to liquids in all cases and gases or vapours where the pressure drop is less than 10% of the upstream pressure. This calculator can also be used for gases or vapours where the pressure drop is up to 40% of the upstream pressure if the average fluid density is used.

The calculator determines the static pressure drop and frictional pressure drop through a line assuming incompressible flow.

Up to 3 pipes of different diameters can be handled in the calculation of the line pressure drop.

  1. Enter the source and destination of the line and the line number
  2. Enter the fluid details and physical properties
  3. Enter the elevations of each end of the line
  4. Choose the nominal diameter and schedule of 1, 2 or all 3 pipes from the drop down lists
  5. The calculator will determine the inside diameter of each selected pipe
  6. Enter a length for 1, 2 or all 3 pipes
  7. Enter an absolute roughness for each pipe. Typical values:
    • Commercial steel: 0.046 mm
    • Drawn tubing (brass, lead, glass): 0.002 mm
    • Asphalted cast iron: 0.122 mm
    • Galvanized iron: 0.152 mm
    • Cast iron: 0.259 mm
  8. Enter the quantities of each type of fitting for each pipe if known
  9. If the type and quantities of each fitting are unknown, enter a fitting factor. Typical factors for 50 metre long lines:
    • 3" diameter and smaller: 1.5
    • 4" and 6" diameter: 2.0
    • 8" diameter and larger: 2.5
  10. Click the "Calculate" button
  11. The calculator will determine the static and frictional pressure drop through 1, 2 or all 3 pipes making up the line
  12. "Reasonable" fluid velocities:
    • Liquids: up to 3 m/s
    • Gases: up to 20 m/s
Line Sizing Diagram
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LINE DETAILS
From  
To  
Line number  
FLUID PROPERTIES
Fluid  
Phase  
Flow rate m
Density ρ
Viscosity μ
ELEVATIONS
Line inlet centreline elevation zin
Line outlet centreline elevation zout
PIPELINES
Pipe 1 Pipe 2 Pipe 3
Pipe nominal diameter inch
Pipe schedule
Pipe internal diameter d 6.8 6.8 6.8 mm
Pipe length L
Absolute roughness e
FITTINGS
Quantities Pipe 1 Pipe 2 Pipe 3
90° LR bends
90° Std elbows
45° LR bends
45° Std elbows
Straight tees (flow thro' run)
Straight tees (flow thro' branch)
Pipe entrances
Pipe exits
Pipe contractions
Pipe expansions
Gate valves
Globe valves
Swing check valves
Lift check valves
Tilting disc check valves
Stop check valves
Poppet foot valves (with strainers)
Hinged disc foot valves (with strainers)
Ball valves
Butterfly valves
Plug valves
 
Miscellaneous losses (no. of velocity heads)
 
Fittings factor
OUTPUTS
Volumetric flow rate Q 100.0
Pipe 1 Pipe 2 Pipe 3
Relative roughness e:d 0.00676 0.00676 0.00676
Flow area A 4e-05 4e-05 4e-05
Velocity u 764.87 764.87 764.87
Reynolds No. Re 5201142 5201142 5201142
Flow regime turbulent turbulent turbulent
Friction factor f 0.03337 0.03337 0.03337
Pipe velocity head loss Kpipe 0.0 0.0 0.0
Fittings total velocity head loss Kfittings 0.0 0.0 0.0
Frictional pressure loss ΔPfriction 0.0 0.0 0.0
Frictional head loss Hfriction 0.0 0.0 0.0
Static pressure loss ΔPstatic 0.0
Static head loss Hstatic 0.0
Total pressure loss ΔPtotal 0.0
Total head loss Htotal 0.0
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