CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > General Forums > Main CFD Forum

Modeling of shear driven flow

Register Blogs Community New Posts Updated Threads Search

Like Tree1Likes
  • 1 Post By ortb

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   February 1, 2023, 02:24
Question Modeling of shear driven flow
  #1
New Member
 
Benjamin Ortner
Join Date: Oct 2021
Location: Graz, Austria
Posts: 9
Rep Power: 5
ortb is on a distinguished road
Dear CFD community,

I have a problem to analyze, which involves a hot gas stream flowing over a surface of molten slag in a container. The question is whether the gas momentum will transfer (at least partly) to the slag to prevent local freezing. Further, we want to get an idea about the shear-driven flow pattern inside the container.

I tried doing it with VOF in Fluent, and it seems to work, although the high viscosity ratio of ~10^5 causes issues. The simulation develops very slow on the slag side and turbulence convergence is bad, probably due to the interpolation of properties (density, viscosity) at the VOF surface.

Another idea I had would be to separate the domains of gas and fluid entirely and use a scheme where I would transfer the wall shear stress of a gas-only simulation as a boundary condition to the slag surface and do it iteratively.

Do you have any advice on how to tackle this properly? Which models would you recommend? Any literature you can think of?

Best regards and thank you for your help!
ortb
ortb is offline   Reply With Quote

Old   February 1, 2023, 05:19
Default
  #2
Senior Member
 
Filippo Maria Denaro
Join Date: Jul 2010
Posts: 6,897
Rep Power: 73
FMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura about
Quote:
Originally Posted by ortb View Post
Dear CFD community,

I have a problem to analyze, which involves a hot gas stream flowing over a surface of molten slag in a container. The question is whether the gas momentum will transfer (at least partly) to the slag to prevent local freezing. Further, we want to get an idea about the shear-driven flow pattern inside the container.

I tried doing it with VOF in Fluent, and it seems to work, although the high viscosity ratio of ~10^5 causes issues. The simulation develops very slow on the slag side and turbulence convergence is bad, probably due to the interpolation of properties (density, viscosity) at the VOF surface.

Another idea I had would be to separate the domains of gas and fluid entirely and use a scheme where I would transfer the wall shear stress of a gas-only simulation as a boundary condition to the slag surface and do it iteratively.

Do you have any advice on how to tackle this properly? Which models would you recommend? Any literature you can think of?

Best regards and thank you for your help!
ortb



Since you have a high viscosity ratio, do you have some experimental/numerical evidence that the stream of gas is able to modify the geometry of the surface of the fluid face by tangential stress?


Would be possible to approximately model the fluid as a solid and work as in CHT problems?
FMDenaro is offline   Reply With Quote

Old   February 1, 2023, 05:44
Default
  #3
New Member
 
Benjamin Ortner
Join Date: Oct 2021
Location: Graz, Austria
Posts: 9
Rep Power: 5
ortb is on a distinguished road
Quote:
Originally Posted by FMDenaro View Post
Since you have a high viscosity ratio, do you have some experimental/numerical evidence that the stream of gas is able to modify the geometry of the surface of the fluid face by tangential stress?

Yes, we are sure that there is in fact a motion. The viscostiy of the slag is not that high at around 0.85 kg/(m-s).


Quote:
Originally Posted by FMDenaro View Post
Would be possible to approximately model the fluid as a solid and work as in CHT problems?

That is exactly what I did as a first approximation. It has shown freezing to a higher degree than is usually observed in such systems. Therfore, we felt that the slag should be modeled as a proper fluid.


Do you think the coupling approach is appropriate?
ortb is offline   Reply With Quote

Old   February 1, 2023, 13:11
Default
  #4
Senior Member
 
Arjun
Join Date: Mar 2009
Location: Nurenberg, Germany
Posts: 1,291
Rep Power: 35
arjun will become famous soon enougharjun will become famous soon enough
Quote:
Originally Posted by ortb View Post
Dear CFD community,

I have a problem to analyze, which involves a hot gas stream flowing over a surface of molten slag in a container. The question is whether the gas momentum will transfer (at least partly) to the slag to prevent local freezing. Further, we want to get an idea about the shear-driven flow pattern inside the container.

I tried doing it with VOF in Fluent, and it seems to work, although the high viscosity ratio of ~10^5 causes issues. The simulation develops very slow on the slag side and turbulence convergence is bad, probably due to the interpolation of properties (density, viscosity) at the VOF surface.

Another idea I had would be to separate the domains of gas and fluid entirely and use a scheme where I would transfer the wall shear stress of a gas-only simulation as a boundary condition to the slag surface and do it iteratively.

Do you have any advice on how to tackle this properly? Which models would you recommend? Any literature you can think of?

Best regards and thank you for your help!
ortb


High viscosity causes high pressure values so any force calculations or momentum flux calculations will be wrong here.


If you are modelling solid region as high viscosity then the results should be wrong.
arjun is offline   Reply With Quote

Old   February 1, 2023, 14:36
Default
  #5
Senior Member
 
Filippo Maria Denaro
Join Date: Jul 2010
Posts: 6,897
Rep Power: 73
FMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura aboutFMDenaro has a spectacular aura about
I think you have no other way that a VOF for the coupled problem, using a very small time-step.
FMDenaro is offline   Reply With Quote

Old   February 2, 2023, 03:13
Default
  #6
New Member
 
Benjamin Ortner
Join Date: Oct 2021
Location: Graz, Austria
Posts: 9
Rep Power: 5
ortb is on a distinguished road
Quote:
Originally Posted by arjun View Post
High viscosity causes high pressure values so any force calculations or momentum flux calculations will be wrong here.


If you are modelling solid region as high viscosity then the results should be wrong.

I think you are right. I found an analytic solution of the shear flow problem, which yields way lower boundary velocities than my simulation.
ortb is offline   Reply With Quote

Old   February 2, 2023, 03:16
Default
  #7
New Member
 
Benjamin Ortner
Join Date: Oct 2021
Location: Graz, Austria
Posts: 9
Rep Power: 5
ortb is on a distinguished road
Quote:
Originally Posted by FMDenaro View Post
I think you have no other way that a VOF for the coupled problem, using a very small time-step.

That is extremely expensive and still does not solve the material property problem. Now I will try to export shear stresses and apply them as a boundary to a second simulation.

Thank you all for your input.
ortb is offline   Reply With Quote

Old   February 2, 2023, 05:20
Default
  #8
Senior Member
 
Arjun
Join Date: Mar 2009
Location: Nurenberg, Germany
Posts: 1,291
Rep Power: 35
arjun will become famous soon enougharjun will become famous soon enough
Quote:
Originally Posted by ortb View Post
I think you are right. I found an analytic solution of the shear flow problem, which yields way lower boundary velocities than my simulation.


We did a ice melting problem long time ago in Wildkatze solver that previously the person tried with fluent and comsol. In both solvers that high viscosity issue created problems. In Wildkatze we then created a method without increasing viscosity. That lead to much better solution.
arjun is offline   Reply With Quote

Old   February 2, 2023, 05:40
Default
  #9
New Member
 
Benjamin Ortner
Join Date: Oct 2021
Location: Graz, Austria
Posts: 9
Rep Power: 5
ortb is on a distinguished road
Quote:
Originally Posted by arjun View Post
We did a ice melting problem long time ago in Wildkatze solver that previously the person tried with fluent and comsol. In both solvers that high viscosity issue created problems. In Wildkatze we then created a method without increasing viscosity. That lead to much better solution.

Fluent is my only realistic option. I will try the workaround via shear stress profiles and report the results.
arjun likes this.
ortb is offline   Reply With Quote

Reply

Tags
multiphase, shear flow, viscosity ratio, vof


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
Questions about FLOW 3D modeling capabilities Dr Youssef Hafez FLOW-3D 0 January 7, 2023 12:37
Is recirculating flow is free vortex or forced vortex? FluidKo Main CFD Forum 11 July 21, 2022 07:21
unable to run dynamic mesh(6dof) and wave UDF shedo Fluent UDF and Scheme Programming 0 July 1, 2022 18:22
Pressure driven flow in 2D LES channelFoam sheaker OpenFOAM Running, Solving & CFD 0 June 26, 2017 15:44
Wall shear stress in channel flow sreeyuth OpenFOAM Running, Solving & CFD 2 September 5, 2014 11:02


All times are GMT -4. The time now is 08:28.