Compressible Flow Pipe Sizing

Calculate pressure drop for compressible (gas) flow through pipes using isothermal or adiabatic flow equations.

Compressible Line Sizing Calculator Guide (PDF)

This calculator determines the pressure drop of a compressible gas or vapour through a pipeline. The calculator can model isothermal and adiabatic flow.

The assumption of compressible flow is reasonable for gases and vapours where the calculated pressure drop is greater than 10% of the upstream pressure.

  1. Enter the line number, source and destination of the line
  2. Select the flow type - isothermal or adiabatic:
    • Isothermal flow is usually assumed for long pipes
    • Adiabatic flow is usually assumed for short, insulated pipes
  3. Enter the fluid details and physical properties
  4. Choose the nominal diameter and schedule of the pipe from the drop down lists, or select "Custom" to enter an internal diameter directly
  5. The calculator will determine the inside diameter of the selected pipe
  6. Enter a length for the pipe
  7. Enter an absolute roughness for the 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 the 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 outlet pressure and the frictional pressure drop through the line
  12. An error will be given if the specified flow rate is too high to be achieved through the pipe with the available pressure drop. In this case:
    • Reduce the flow rate
    • Increase the pipe diameter
    • Increase the inlet pressure
Log in to save and load calculations
LINE DETAILS
Line number  
Source  
Destination  
FLOW TYPE
Type of flow  
FLUID PROPERTIES
Fluid  
Flowrate m
Inlet density ρ1
Viscosity μ
Inlet temperature T1
Inlet pressure P1
Ratio of specific heat capacities γ
PIPELINE
Pipe nominal diameter   inch
Pipe schedule  
Pipe internal diameter d 6.8 mm
Pipe length L
Absolute roughness e
FITTINGS
  Quantity
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
Relative roughness e:d
Flow area A
Reynolds No. Re
Flow regime  
Friction factor f
Pipe velocity head loss Kpipe
Fittings total velocity head loss Kfittings
  Inlet Outlet  
Mach number Mach
Temperature T
Density ρ
Volumetric flow rate Q
Velocity u
Pressure P
Critical velocity ucritical
Choked flow?  
Outlet pressure P2
Pressure drop through pipe ΔP
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