|
[Sponsors] |
October 9, 2014, 17:06 |
non newtonian viscosity
|
#1 |
New Member
mina
Join Date: Nov 2013
Posts: 20
Rep Power: 13 |
Hi
To calculate the average velocity of ostwald de waele fluid flow at Re=50 as an inlet boundary, i need to write an expression for its viscosity first. can anybody help me to write this according m,n,max & min shear strain rate? is it possible? thanks |
|
October 9, 2014, 18:58 |
|
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
If you know the viscosity function and parameters then why can't you calculate the viscosity?
|
|
October 10, 2014, 02:34 |
|
#3 |
New Member
mina
Join Date: Nov 2013
Posts: 20
Rep Power: 13 |
Because of shear strain rate. In ostwald fluid we define max & min for shear strain rate so we have a span for it not a constant value.
|
|
October 10, 2014, 02:40 |
|
#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
You can access the shear strain rate variable in CFX, then you could use this in your calculation. This would make the boundary condition a function of the flow domain but often this sort of coupling works OK.
Alternately you could just estimate the SSR, maybe from a simple pipe flow or something with a simpler answer. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Problem with divergence | TDK | FLUENT | 13 | December 14, 2018 07:00 |
Ratio of eddy viscosity to molecular viscosity : Laminar or turbulent flow? | JuPa | CFX | 7 | September 9, 2013 08:45 |
Non newtonian viscosity UDF -Diveregence in AMG Solver error | Josyula | Fluent UDF and Scheme Programming | 4 | March 19, 2013 01:05 |
non newtonian viscosity problem | moloykb | FLUENT | 4 | July 5, 2012 16:47 |
Too low temperature at combustor outlet | romekr | FLUENT | 2 | February 6, 2012 11:02 |