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

simulate nanofluids with mixture model

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   April 27, 2023, 05:44
Default simulate nanofluids with mixture model
  #1
New Member
 
rasoul rezazadeh
Join Date: Apr 2023
Posts: 3
Rep Power: 3
rasoul1375 is on a distinguished road
hello. I want to simulate cuo nanoparticles dispersed in 60:40 Eg/W base fluid with mixture model. I defined 2 fluid materials for base fluid and cuo nanoparticles but I don't know what value to set for viscosity of cuo! Should I set it to zero?
and also should I activate the granular option for it? I tried both ways, but after running, the viscosity of the mixture is wrong and it is almost equal to the viscosity of the base fluid. what should I do?
rasoul1375 is offline   Reply With Quote

Old   April 27, 2023, 06:15
Default
  #2
Senior Member
 
Join Date: Jun 2009
Location: Technische Universität Chemnitz
Posts: 107
Rep Power: 17
NickFL is on a distinguished road
The nanoparticles are dispersed in the water/ethylene glycol mixture. The solid particles themselves do not have viscosity perse. The liquid mixture will of course. Generally nanoscale size particles will follow the flow very well unless acted upon by an outside source. If you are setting your model up with Copper Oxide nanoparticles as a component in a mixture, leave it to what your use for the liquid mixture.



What is the particle loading in your model? How are you attempting to model the particles? Will you be using the Population Balance models? What are you attempting to see in the results? All of these really go to answering the question.
NickFL is offline   Reply With Quote

Old   April 27, 2023, 06:41
Default
  #3
New Member
 
rasoul rezazadeh
Join Date: Apr 2023
Posts: 3
Rep Power: 3
rasoul1375 is on a distinguished road
Quote:
Originally Posted by NickFL View Post
The nanoparticles are dispersed in the water/ethylene glycol mixture. The solid particles themselves do not have viscosity perse. The liquid mixture will of course. Generally nanoscale size particles will follow the flow very well unless acted upon by an outside source. If you are setting your model up with Copper Oxide nanoparticles as a component in a mixture, leave it to what your use for the liquid mixture.



What is the particle loading in your model? How are you attempting to model the particles? Will you be using the Population Balance models? What are you attempting to see in the results? All of these really go to answering the question.
I am simulating an article about the use of nanofluids inside the car radiator. I use the two-phase mixture model and I have set the Population balance model to off (of course, I am not familiar with it and I don't know if it should be on or off), I considered the inlet velocity for the base fluid and nanoparticles to be equal, and the Reynolds at the inlet is almost equal to 200 and I used the outlet pressure boundary condition for the outlet. I considered the convection boundary condition on the walls. I am looking for changes in Cf and h in the results. When I set the viscosity of cuo to zero, the viscosity of the mixture after running is different from the number reported by the article (of course, the article solved it in a single phase, but I want to reach the results from the two-phase mixture model)
What are your recommendations for simulating nanoparticles in the mixture method?
rasoul1375 is offline   Reply With Quote

Old   April 27, 2023, 13:15
Default
  #4
Senior Member
 
Join Date: Jun 2009
Location: Technische Universität Chemnitz
Posts: 107
Rep Power: 17
NickFL is on a distinguished road
Do you know how the changes in viscosity and heat conductivity will change as a function of particle loading? For what you mention, I do not see any reason to explicitly model the particles. It would simply be different simulations with different material properties based upon the amount of CuO in the stream. Is there a reason why you need to include the particles?
NickFL is offline   Reply With Quote

Reply

Tags
cuo, fluen, mixture model, nanofluid, tow phase model


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
interFoam wave propagation and explosion of Courant number and residuals ChiaraViola OpenFOAM Running, Solving & CFD 1 June 26, 2019 06:36
Mixture model problem - could someone please advise? matlab_monkey FLUENT 2 July 26, 2012 09:20
Modelling Sand erosion using Mixture model and DPM karlchapman FLUENT 3 July 5, 2012 09:55
species transport model or mixture model? achaokaoyan Main CFD Forum 0 July 10, 2010 11:52
PDF combustion model to simulate reaction of gas i Mark FLUENT 0 August 4, 2001 12:07


All times are GMT -4. The time now is 23:55.