Two Phase Pressure Drop in Piping

Important Notices:
 
bulletThe frictional pressure drop calculation presented here applies to steady-state, isothermal two phase pipe flow of incompressible Newtonian fluids. The procedure is based on the "Baker" correlations and flow regime maps. The procedure automatically handles the complete range of industrially used steel pipe sizes and schedules.
bulletA more comprehensive and powerful version of this procedure is available online through the Process Associate's clients gateway (password required). WWW-based and stand-alone versionsof the full program for Windows 3.1x/95/NT and Unix operating systems are available through their coordination office. The full version of this procedure is part of their Process Designer® line of intelligent software.
bulletFor your convenience, The input form below has several multiple choice fields {using radio buttons} with one field already selected as default. Please make sure that you always mark the proper button corresponding to your input if it is different from the default.
Gas / Vapor Flowrate
  Mass Basis
Volume Basis
Superficial Velocity Basis

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Gas / Vapor Physical Properties
  Density
Viscosity

dp_2.gif (6069 bytes)

Liquid Flowrate
  Mass Basis
Volume Basis
Superficial Velocity Basis

dp_2.gif (6069 bytes)

Liquid Physical Properties
  Density
Viscosity
Surface Tension

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Piping
Orientation
Length
Diameter Nominal, inches (1) Schedule(2)
Inside / equivalent

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Report:

Pressure Drop in

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Notes:

  1. For commercial steel pipes only.
  2. The schedule list is all inclusive. Hence, some of the pipe schedules shown are not available for every nominal pipe size. If you select an invalid nominal pipe size and schedule combination, the server will return a list showing which schedules are available for the nominal pipe size you specified. We apologize for this awkward behavior but it is due to current HTML and browser technology limitations.

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