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

Results not matching for transient thermal natural convection case fluent

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 11, 2017, 09:34
Default Results not matching for transient thermal natural convection case fluent
  #1
New Member
 
Nitin Suryawanshi
Join Date: Mar 2009
Location: Pune, India
Posts: 28
Rep Power: 17
suryawanshi_nitin is on a distinguished road
Hello All,
I am working on transient thermal problem for which i have carried out experiment at home as explained below,
1. Coke placed at center of room with Coke can temperature 74 Deg. C initially.
2. Ambient temperature of room is 26 deg. C.
3. Started monitoring temp of Coke can for 1 hour which is filled with water & can was closed at top. Thermometer inserted till mid height of can.
4. Temperature of Coke can observed after 1 hour was 44 Deg. C. Hence coke can temperature has dropped from 66 to 44 Deg. C in one hour experimentally.

Then same setup i have created in CFD by creating 3D model of closed room with Coke can at center. Hex mesh created in domain (ICEM block Mesh) & also the boundary layer around can (with Y+<1). Transient, segregated solver selected with SST-kW model turbulence model, also 2nd order scheme for flow equations & also for transient formulation was selected. Density modeled with boussinesq approx. After running transient thermal simulation in Fluent 14.5 version it was observed fluent took more than 3+ hours to drop coke can temperature from 66 to 44 Deg. C.
Hence, why fluent (CFD solvers) taking more time (>3+ hours) than experimental measured time (1 hour) ?
Do i need to use some other settings ?
Thank you in advance.
suryawanshi_nitin is offline   Reply With Quote

Old   March 11, 2017, 15:53
Default
  #2
Senior Member
 
Lucky
Join Date: Apr 2011
Location: Orlando, FL USA
Posts: 5,754
Rep Power: 66
LuckyTran has a spectacular aura aboutLuckyTran has a spectacular aura aboutLuckyTran has a spectacular aura about
Two sanity checks you can do.

1). Compare the heat transfer coefficient you obtained from your Fluent simulation w/ that observed experimentally (you need to back-calculate it).

2). Solve only the transient heat transfer inside the can with the heat transfer coefficient prescribed equal to the heat transfer coefficient you get from your experiment. If it still takes 3 hours, then you know it's the heat transfer inside the can that is not being correctly modelled and not the natural convection outside the can.

Finally. How are you modelling the water in the can? Is it a fluid or solid? If you model it as a solid, then you don't get convection inside the can which would slow the rate of heat transfer.
LuckyTran is offline   Reply With Quote

Reply

Tags
transient thermal


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
[DesignModeler] DesignModeler Scripting: How to get Full Command Access ANT ANSYS Meshing & Geometry 53 February 16, 2020 16:13
Unusual results for a multiphase case in fluent Sadegh.A FLUENT 0 November 9, 2015 19:27
Error in reading Fluent 13 case file in fluent 12 apurv FLUENT 2 July 12, 2013 08:46
Free surface boudary conditions with SOLA-VOF Fan Main CFD Forum 10 September 9, 2006 13:24
Info: Short Course On Thermal Design of Electronic Equipment Arnold Free Main CFD Forum 0 August 10, 1999 11:18


All times are GMT -4. The time now is 13:54.