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

FLUENT Mixture model for Nanofluid

Register Blogs Community New Posts Updated Threads Search

Like Tree6Likes
  • 2 Post By micro77
  • 2 Post By Goutam
  • 1 Post By Goutam
  • 1 Post By HyperNova

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   March 24, 2012, 17:21
Question FLUENT Mixture model for Nanofluid
  #1
New Member
 
Waqas Ahmed
Join Date: Feb 2011
Posts: 18
Rep Power: 15
Waqas Ahmed is on a distinguished road
Hi,

Can Mixture model (FLUENT) can be used for simulation of nanofluid?
I've heard that mixture model is for particles of micro in size.
Waqas Ahmed is offline   Reply With Quote

Old   March 26, 2012, 04:18
Default
  #2
New Member
 
diah hidayanti
Join Date: Mar 2012
Posts: 1
Rep Power: 0
diah is on a distinguished road
I have the same question with Waqas Ahmed. I plan to use FLUENT for simulation of nanofluid heat transfer, but i'm not sure the mixture model is applicable for nano-sized particle.




Quote:
Originally Posted by Waqas Ahmed View Post
Hi,

Can Mixture model (FLUENT) can be used for simulation of nanofluid?
I've heard that mixture model is for particles of micro in size.
diah is offline   Reply With Quote

Old   March 29, 2012, 12:57
Question what s the meaning of sum of volume fraction in montoring?
  #3
New Member
 
rz
Join Date: Mar 2012
Posts: 25
Rep Power: 0
rezacfd1361 is on a distinguished road
what s the meaning of selecting sum in "define surface monitor" for "Phrases" , "volume fraction" . I have a 2 phase domain, primary phase is air and secondary phase is water. I am going to track surface changes for water, in internet i read that I have to select sum when i intoduce monitors/surface/surface monitors/define surface monitor.
my case is a Neumerical Wave Tank.
please help me.
rezacfd1361 is offline   Reply With Quote

Old   September 29, 2012, 08:23
Default yes we can and i do this work ms.khalafi@yahoo.com please contact with me
  #4
New Member
 
sadegh
Join Date: Jul 2011
Posts: 2
Rep Power: 0
parsad is on a distinguished road
Quote:
Originally Posted by Waqas Ahmed View Post
Hi,

Can Mixture model (FLUENT) can be used for simulation of nanofluid?
I've heard that mixture model is for particles of micro in size.
yes we can and i do this work ms.khalafi@yahoo.com please contact with me
parsad is offline   Reply With Quote

Old   October 12, 2012, 21:59
Default mixture model for nanofluid
  #5
New Member
 
micro77
Join Date: Dec 2011
Posts: 5
Rep Power: 15
micro77 is on a distinguished road
Dear all,

I'm simulating nanofluid (Alumina water-based) using mixture model. The primary phase (water) and the secondary phase (alumina-2%). Eventhough the volume fraction of alumina is very small, the particle diameter is larger enough compared to water.

dia. of water molecule=0.29 nm, dia. of alumina=20 - 40 nm.

In mixture model, i'm defining both properties as individual property(not mixture properties). What make me confuse here is that from lit. review, all papers shows the eff. thermal properties (mixture properties) instead of individual properties.

Am I doing wrong here?Should i define the mixture or individual properties? In fluent tutorial, they use individual properties.

Thanks in advance
micro77 is offline   Reply With Quote

Old   October 9, 2013, 07:46
Default
  #6
Senior Member
 
Goutam Saha
Join Date: Dec 2011
Location: UK
Posts: 131
Rep Power: 15
Goutam is on a distinguished road
Quote:
Originally Posted by micro77 View Post
Dear all,

I'm simulating nanofluid (Alumina water-based) using mixture model. The primary phase (water) and the secondary phase (alumina-2%). Eventhough the volume fraction of alumina is very small, the particle diameter is larger enough compared to water.

dia. of water molecule=0.29 nm, dia. of alumina=20 - 40 nm.

In mixture model, i'm defining both properties as individual property(not mixture properties). What make me confuse here is that from lit. review, all papers shows the eff. thermal properties (mixture properties) instead of individual properties.

Am I doing wrong here?Should i define the mixture or individual properties? In fluent tutorial, they use individual properties.

Thanks in advance
I have the same problem, how to use mixture model for nanofluids in Fluent?
TRINAVEE and thakuramit682 like this.
Goutam is offline   Reply With Quote

Old   December 15, 2014, 17:42
Default
  #7
Senior Member
 
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12
HyperNova is on a distinguished road
hi , could any body here solve the problem with mixture model in nanofluid modelling ? thanks
HyperNova is offline   Reply With Quote

Old   February 24, 2015, 04:35
Default
  #8
New Member
 
saurabh gupta
Join Date: Jun 2014
Posts: 9
Rep Power: 12
saurabhg2014 is on a distinguished road
You found any solution?
saurabhg2014 is offline   Reply With Quote

Old   February 25, 2015, 23:51
Default
  #9
Senior Member
 
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12
HyperNova is on a distinguished road
who ? me ?!
HyperNova is offline   Reply With Quote

Old   February 26, 2015, 01:59
Default
  #10
New Member
 
saurabh gupta
Join Date: Jun 2014
Posts: 9
Rep Power: 12
saurabhg2014 is on a distinguished road
Quote:
Originally Posted by HyperNova View Post
who ? me ?!
yes , if you succeeded then?
saurabhg2014 is offline   Reply With Quote

Old   June 8, 2015, 03:40
Default
  #11
Senior Member
 
Goutam Saha
Join Date: Dec 2011
Location: UK
Posts: 131
Rep Power: 15
Goutam is on a distinguished road
You can see this paper:
http://www.sciencedirect.com/science...3519331400284X
Mixture model in FLuent has been used for nanofluid.
HyperNova likes this.
Goutam is offline   Reply With Quote

Old   July 10, 2015, 03:58
Default
  #12
New Member
 
Join Date: Jul 2015
Posts: 4
Rep Power: 11
TRINAVEE is on a distinguished road
WHERE CAN THE PARTICLE VOLUME CONCENTRATION eg 1% ,4% BE given FOR NANO FLUID here in fluent ?
TRINAVEE is offline   Reply With Quote

Old   July 10, 2015, 04:00
Default
  #13
New Member
 
Join Date: Jul 2015
Posts: 4
Rep Power: 11
TRINAVEE is on a distinguished road
i have the same doubt .please help
TRINAVEE is offline   Reply With Quote

Old   March 23, 2016, 06:52
Default
  #14
New Member
 
Rajendra Singh
Join Date: Aug 2015
Posts: 16
Rep Power: 11
rajann_786 is on a distinguished road
Please refer this
http://www.sciencedirect.com/science/article/pii/S1290072912003420
rajann_786 is offline   Reply With Quote

Old   April 25, 2017, 17:15
Default
  #15
New Member
 
sinemdiscioglu
Join Date: Apr 2017
Posts: 2
Rep Power: 0
sinemdiscioglu is on a distinguished road
hello can you help me?
sinemdiscioglu is offline   Reply With Quote

Old   March 16, 2019, 01:33
Default
  #16
New Member
 
mohammad faizan
Join Date: Apr 2017
Posts: 5
Rep Power: 9
mohammad faizan is on a distinguished road
Quote:
Originally Posted by micro77 View Post
Dear all,

I'm simulating nanofluid (Alumina water-based) using mixture model. The primary phase (water) and the secondary phase (alumina-2%). Eventhough the volume fraction of alumina is very small, the particle diameter is larger enough compared to water.

dia. of water molecule=0.29 nm, dia. of alumina=20 - 40 nm.

In mixture model, i'm defining both properties as individual property(not mixture properties). What make me confuse here is that from lit. review, all papers shows the eff. thermal properties (mixture properties) instead of individual properties.

Am I doing wrong here?Should i define the mixture or individual properties? In fluent tutorial, they use individual properties.

Thanks in advance
@gautam did u solve ur problem?
mohammad faizan is offline   Reply With Quote

Old   March 16, 2019, 04:53
Default
  #17
Senior Member
 
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12
HyperNova is on a distinguished road
if the volume fraction is less than 2 percent, DPM can be used in my opinion. But one should be careful with interfacial forces like drag law.
mghr likes this.
HyperNova is offline   Reply With Quote

Reply


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
mixture model for cavitation mech5190 FLUENT 12 December 7, 2016 04:24
Superlinear speedup in OpenFOAM 13 msrinath80 OpenFOAM Running, Solving & CFD 18 March 3, 2015 06:36
Mixture model validation cases Antoine Main CFD Forum 1 January 24, 2011 02:02
multi fluid mixture model issue rystokes CFX 3 August 9, 2009 20:13
Advanced Turbulence Modeling in Fluent, Realizable k-epsilon Model Jonas Larsson FLUENT 5 March 13, 2000 04:27


All times are GMT -4. The time now is 23:06.