|
[Sponsors] |
March 30, 2012, 14:09 |
gas-liquid slug flow in horizontal pipe
|
#1 |
New Member
zainab
Join Date: Mar 2012
Posts: 17
Rep Power: 14 |
Hello every one, I am a new member. I working on Fluent for modeling a two-phase, gas-liquid (air-water) slug flow in a pipe and I need some help please. My case: pipe length (583cm), (1.27cm) diameter, drawing and meshing by Gambit, the total elements was (112896 cell(, the pipe inlet set to (velocity-inlet), outlet to (outflow), pipe surface to (wall), the pipe continuum to (fluid). In fluent the define sequence as: 1. Solver: pressure based, unsteady, implicit scheme. 2. Multiphase: VOF. 3. Viscous: k-epsilon, standard. 4. Phases: primary as water, secondary as air, interaction: wall adhesion, surface tension (0.07). 5. Operating condition: gravity at y (-9.81), specified operating density. 6. Boundary condition: a. mixture velocity (1.6), k(0.025), epsilon(0.0072). b. air – multiphase volume fraction (1). 7. Initialize: vf=0.18, patch: air vf =0.18. I have a problem I need to get the contour of the slug vf, volume fraction? And, do I need to use a UDF for the velocity?[/FONT]
|
|
Tags |
gas-liquid, horizontal pipe, slug, two-phase, volume fraction |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Slug flow in a vertical pipe | Abe | FLUENT | 0 | March 29, 2007 09:01 |
gas solid pipe flow | tahar | Phoenics | 6 | November 3, 2003 12:03 |
Gas Liquid flow in a packed column | Rakib | FLUENT | 8 | June 18, 2002 01:58 |
fluid flow fundas | ram | Main CFD Forum | 5 | June 17, 2000 21:31 |
Hydrostatic pressure in 2-phase flow modeling (long) | DS & HB | Main CFD Forum | 0 | January 8, 2000 15:00 |