Solid fraction proflie about Eulerian model

wangjihong0407 · October 12, 2010, 13:03

Hello,
Recently I have used Eulerian Model to calculate the horizontal pipe flow about solid-liquid flow. The flow is laminar and steady.But I found some questions during the simulation. I found the solid fraction profile at the top of the pipe is unsteady. That is to say, When the solid phase velocity profile is steady during the fully developed flow region, the fraction of solid phase profile is not steady. And it changes along the pipeline. I am confused. How can I get the steady result ?
Thanks in advance!

Jihong Wang

kondora · October 12, 2010, 14:39

If you are using steady solver - it seems that this is solution convergence problem - possible solution: refine the mesh and/or use higher discretization schemes. Solution may behave unsteady when using steady solver when the physical phenomena being under consideration is physically unsteady (i.e. is unsteady in reality). I'd rather recommend to use unsteady solver and average solution using flow statistics. Hope this helps.

wangjihong0407 · October 14, 2010, 02:21

Kondora,

Thanks for your advice. I will try it.

sandisk · July 17, 2011, 16:27

Hi, even i am trying to work on simulation of slurry flow in horizontal pipeline. I was wondering what were the boundary conditions you used. Was it velocity inlet and pressure outlet. And did you use, Unsteady state solver ? Your reply would be greatly appreciated.Thanks.

October 12, 2010, 13:03	Solid fraction proflie about Eulerian model	#1
wangjihong0407 New Member Jihong Wang Join Date: Mar 2010 Posts: 2 Rep Power: 0	Hello, Recently I have used Eulerian Model to calculate the horizontal pipe flow about solid-liquid flow. The flow is laminar and steady.But I found some questions during the simulation. I found the solid fraction profile at the top of the pipe is unsteady. That is to say, When the solid phase velocity profile is steady during the fully developed flow region, the fraction of solid phase profile is not steady. And it changes along the pipeline. I am confused. How can I get the steady result ? Thanks in advance! Jihong Wang

Similar Threads
Thread	Thread Starter	Forum	Replies	Last Post
Error message: Insufficient Catalogue Size	Paresh Jain	CFX	33	August 16, 2024 06:09
Puzzling about the "diameter" in Eulerian Model	yuanyuan	FLUENT	2	October 22, 2009 09:38
One-way coupling in Eulerian -Eulerian model	swati_mohanty	FLUENT	0	October 8, 2009 01:44
Eulerian Model	Hassan	FLUENT	1	September 4, 2006 09:02
Packing limit management in the Eulerian model	ap	FLUENT	2	September 16, 2005 18:46

October 12, 2010, 14:39		#2
kondora New Member Grzegorz Kondora Join Date: Oct 2010 Posts: 13 Rep Power: 16	If you are using steady solver - it seems that this is solution convergence problem - possible solution: refine the mesh and/or use higher discretization schemes. Solution may behave unsteady when using steady solver when the physical phenomena being under consideration is physically unsteady (i.e. is unsteady in reality). I'd rather recommend to use unsteady solver and average solution using flow statistics. Hope this helps.

October 14, 2010, 02:21		#3
wangjihong0407 New Member Jihong Wang Join Date: Mar 2010 Posts: 2 Rep Power: 0	Kondora, Thanks for your advice. I will try it.

July 17, 2011, 16:27		#4
sandisk New Member sunny Join Date: Jan 2011 Posts: 29 Rep Power: 15	Hi, even i am trying to work on simulation of slurry flow in horizontal pipeline. I was wondering what were the boundary conditions you used. Was it velocity inlet and pressure outlet. And did you use, Unsteady state solver ? Your reply would be greatly appreciated.Thanks.