|
[Sponsors] | |||||
|
|
|
#1 |
|
New Member
Join Date: Oct 2015
Posts: 6
Rep Power: 12 ![]() |
Hello,
I am simulating a laminar (actually with Re<<1) flow between two parallel plates (2D model). I am trying a convergence study by computing the pressure drop as function of the mesh size: well, refining the mesh I get lower and lower pressure drops, and an increasing difference with the theoretical value which is higher. Surprisingly only a coarse mesh gives me a value close to the theoretical one. I am using: - velocity inlet, pressure outlet BCs, - a quadrilateral mesh refined at the boundaries (bias factor), - fully developed velocity profile extracted from a previous calculation on the same mesh, - 1e-6 residuals, QUICK scheme for momentum, second order for pressure (checked may schemes, no differences). Can anybody help me please? Thanks a lot |
|
|
|
|
|
|
|
|
#2 |
|
New Member
Join Date: Oct 2015
Posts: 6
Rep Power: 12 ![]() |
the velocity profile is correct...I don't know the problem...
|
|
|
|
|
|
![]() |
| Thread Tools | Search this Thread |
| Display Modes | |
|
|
Similar Threads
|
||||
| Thread | Thread Starter | Forum | Replies | Last Post |
| [mesh manipulation] Importing Multiple Meshes | thomasnwalshiii | OpenFOAM Meshing & Mesh Conversion | 18 | December 19, 2015 19:57 |
| How to study pressure drop of continous phase in VOF model | sajeesh | FLUENT | 4 | February 5, 2014 23:01 |
| Pressure Drop Calculation | mk_mard | STAR-CCM+ | 3 | August 29, 2011 03:06 |
| a problem in calculating pressure drop in Fluent? | yu chun | FLUENT | 1 | May 18, 2004 04:40 |
| Hydrostatic pressure in 2-phase flow modeling (CFX4.2) | HB &DS | CFX | 0 | January 9, 2000 14:19 |