CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > FLUENT

Submerged intake: Reverse flow in inlet outlet, turbulent viscosity limited

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   September 13, 2019, 08:08
Post Submerged intake: Reverse flow in inlet outlet, turbulent viscosity limited
  #1
New Member
 
Join Date: Feb 2019
Posts: 1
Rep Power: 0
CFDblast is on a distinguished road
Hi all,

I am new using ansys fluent. For my thesis project my task is to analyse a NACA submerged inlet in cruise conditions: 39000 ft, Mach 0.8.

Due to the shape of the inlet, a pair of vortices will be generated. For this type of submerged intake, it is important that the boundary layer is accurately resolved. This is the reason that I've applied an inflation layer at every physical wall.

The computational domain is divided into 7 parts. See file attached. The incoming air goes from right to left. The upper part consists of 3 blocks. Mapped mesh has been applied to those blocks. For the 3 blocks near the fuselage which is a physical wall, which is an inflation layer, the blocks are filled with tetrahedrons. Ansys doesn't allow mapped mesh and inflation layer, so I use tetredrons. For the last part, which is the duct downstream of the submerged intake, somehow an inflation layer can be combined with a mapped mesh. Since it works, I left it as it is. The inlet and outlet are around 6-7 times characteristic length of the submerged intake away from the submerged intake in the middle of the domain. The mesh consists of 5.6M cells.

The boundary conditions are as follows: pressure inlet, pressure outlet, pressure outlet with target mass flow (at the end of the duct downstream of the submerged intake), the far-field is a free slip-wall. For the simulation I changed the pressure outlet with target mass flow as wall.

I've tried to run different simulations at other conditions: 0 ft, Mach 0.20, such that it is faster to check if the settings are correct or not. I've run laminar, k-e, k-omega models.

The errors (log file attached) that are shown during the simulation are:

reversed flow in xxxx faces on pressure-inlet 6.
reversed flow in xxxx faces on pressure-outlet 7.
turbulent viscosity limited to viscosity ratio of 1.000000e+05 in xxxxxxx cells
Stabilizing pressure correction to enhance linear solver robustness.

Divergence detected in AMG solver: k
Divergence detected in AMG solver: omega
Error at host: floating point exception
Error at Node 0: floating point exception
Error: floating point exception
Error Object: #f


And then the simulation aborts.

Does anyone know the reason why it went wrong, or anyone that has tips on mesh/solving those problems?

Thanks in advance!

Steve
Attached Images
File Type: png mesh.PNG (69.8 KB, 13 views)
Attached Files
File Type: txt logfile.txt (72.6 KB, 3 views)
CFDblast is offline   Reply With Quote

Reply

Tags
naca intake, reversed flow, submerged intake


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
3D CFD simulation of propeller blade - Turbulent viscosity limited to viscosity ratio Quentin_C FLUENT 1 April 4, 2017 06:32
Compressible flow, no data at the outlet mireis FLUENT 6 September 3, 2015 03:10
Mass flow inlet and pressure outlet issue nikhil FLUENT 5 December 11, 2013 13:30
Couple outlet to inlet to achieve a fully developed flow. raghu.tejaswi Fluent UDF and Scheme Programming 8 July 18, 2013 10:04
CFDesign V11 -- Reverse flow at outlet maruthiv Autodesk Simulation CFD 1 June 17, 2011 10:38


All times are GMT -4. The time now is 13:29.