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March 24, 2012, 17:21 |
FLUENT Mixture model for Nanofluid
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#1 |
New Member
Waqas Ahmed
Join Date: Feb 2011
Posts: 18
Rep Power: 15 |
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. |
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March 26, 2012, 04:18 |
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#2 |
New Member
diah hidayanti
Join Date: Mar 2012
Posts: 1
Rep Power: 0 |
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.
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March 29, 2012, 12:57 |
what s the meaning of sum of volume fraction in montoring?
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#3 |
New Member
rz
Join Date: Mar 2012
Posts: 25
Rep Power: 0 |
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. |
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September 29, 2012, 08:23 |
yes we can and i do this work ms.khalafi@yahoo.com please contact with me
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#4 | |
New Member
sadegh
Join Date: Jul 2011
Posts: 2
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Quote:
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October 12, 2012, 21:59 |
mixture model for nanofluid
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#5 |
New Member
micro77
Join Date: Dec 2011
Posts: 5
Rep Power: 15 |
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 |
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October 9, 2013, 07:46 |
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#6 | |
Senior Member
Goutam Saha
Join Date: Dec 2011
Location: UK
Posts: 131
Rep Power: 15 |
Quote:
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December 15, 2014, 17:42 |
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#7 |
Senior Member
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12 |
hi , could any body here solve the problem with mixture model in nanofluid modelling ? thanks
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February 24, 2015, 04:35 |
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#8 |
New Member
saurabh gupta
Join Date: Jun 2014
Posts: 9
Rep Power: 12 |
You found any solution?
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February 25, 2015, 23:51 |
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#9 |
Senior Member
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12 |
who ? me ?!
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February 26, 2015, 01:59 |
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#10 |
New Member
saurabh gupta
Join Date: Jun 2014
Posts: 9
Rep Power: 12 |
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June 8, 2015, 03:40 |
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#11 |
Senior Member
Goutam Saha
Join Date: Dec 2011
Location: UK
Posts: 131
Rep Power: 15 |
You can see this paper:
http://www.sciencedirect.com/science...3519331400284X Mixture model in FLuent has been used for nanofluid. |
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July 10, 2015, 03:58 |
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#12 |
New Member
Join Date: Jul 2015
Posts: 4
Rep Power: 11 |
WHERE CAN THE PARTICLE VOLUME CONCENTRATION eg 1% ,4% BE given FOR NANO FLUID here in fluent ?
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July 10, 2015, 04:00 |
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#13 |
New Member
Join Date: Jul 2015
Posts: 4
Rep Power: 11 |
i have the same doubt .please help
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March 23, 2016, 06:52 |
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#14 |
New Member
Rajendra Singh
Join Date: Aug 2015
Posts: 16
Rep Power: 11 |
Please refer this
http://www.sciencedirect.com/science/article/pii/S1290072912003420 |
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April 25, 2017, 17:15 |
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#15 |
New Member
sinemdiscioglu
Join Date: Apr 2017
Posts: 2
Rep Power: 0 |
hello can you help me?
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March 16, 2019, 01:33 |
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#16 | |
New Member
mohammad faizan
Join Date: Apr 2017
Posts: 5
Rep Power: 9 |
Quote:
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March 16, 2019, 04:53 |
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#17 |
Senior Member
B_Kia
Join Date: May 2014
Location: Ir
Posts: 123
Rep Power: 12 |
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.
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