Two Phase Pressure Drop in Piping
![]()
| The 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. | |
| A 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. | |
| For 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 | ||
|
||
| Gas / Vapor Physical Properties | ||
| Density | ||
| Viscosity | ||
|
||
| Liquid Flowrate | ||
| Mass Basis | ||
| Volume Basis | ||
| Superficial Velocity Basis | ||
|
||
| Liquid Physical Properties | ||
| Density | ||
| Viscosity | ||
| Surface Tension | ||
|
||
| Piping | ||
| Orientation | ||
| Length | ||
| Diameter | Nominal, inches (1) | Schedule(2) |
| Inside / equivalent | ||
|
||
| Report: | ||
Pressure Drop in |
||
|
||
![]()
![]()
Copyright © 1996, Process Associates of America. All Rights Reserved.