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Non newtonian pressure drop

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Lijantropo

Chemical
Jun 26, 2009
56
Good morning,

I have to pump a non-newtonian fluid (an emulsion). I know some lab properties of the fluids (enough to estimate the apparent viscosity) but I'm not sure of what set of equations I should use. Do you have any good reference where I can find simplified equations for make a good estimation of pressure drop in pipes for this kind of fluids?

(pd: I have read some papers where the autors suggest to use the same equations for newtonian and non-newtonian fluis, changing only the viscosity. What do you think?)

Regards,

lij.
 
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It depends. What is the rheology of the fluid? Most, but not all, emulsions are shear thinning.

Good luck,
Latexman
 
Hi,
You're right Mr Latexman, it is shear-thinning.
lij
 
Then as long as the shear rate created in the pipe is greater than the shear rate of the lab viscosity measurements, using the lab viscosity in a Newtonian method is conservative.

I gave an excellent reference a while back. Do a search here and in the Chemical Engineering forums and see if you find it. If not, let me know and I'll repeat it. It was a series of articles in Chemical Engineering Magazine.

Good luck,
Latexman
 
BI,

Agree. If one takes the easy way out, there is usually a catch!

Good luck,
Latexman
 
For the most part you just need to formulate some equation to relate viscosity to (normally via shear to) vs velocity.

It gets tricker if your viscosity varies with time at various velocities, or has other more devious complications.

"I am sure it can be done. I've seen it on the internet." BigInch's favorite client.

"Being GREEN isn't easy." Kermit[frog]
 
Lijantropo,

Look here:

thread378-243822

Good luck,
Latexman
 
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